PROCESS FOR THE PRODUCTION OF AZIRIDINES Field of the Invention

This invention relates to a process for the production of aziridines. More specifically, this invention relates to a process for converting a 3-hydroxyamine to the corresponding aziridine by contacting the amine with molecular sieves loaded with certain metals. The process of the invention is particularly, though not exclusively, intended for the conversion of monoethanolamine to ethylenimine. Background of the Invention

Ethylenimine is a potential chemical intermediate for the production of linear ethyleneamine polymers and for the production of various other amines. However, because of the toxicity and carcinogenicity of ethylenimine, this material poses severe handling difficulties, which make it highly undesirable to store or transport the ethylenimine, so that, desirably a process for the production of ethylenimine should begin from inexpensive starting materials, and should provide the ethylenimine in a form which permits its direct feed to the ethyleneamine production unit without intervening isolation or storage of the ethylenimine.

Various processes for the production of ethylenimine are knovm. For example, ethylenimine may be produced by the reaction of ethylene dichloride with anhydrous ammonia. However, this method suffers from

the disadvantages of involving halide use and producing a salt by-product.

One commercially attractive process for the production of ethylenimine is the catalytic dehydration of monoethanolamine. Various catalysts capable of effecting this dehydration are known; most of the known catalysts are oxides of tungsten, tantalum or niobium, in some cases promoted with transition metals such as iron or chromium, the metal oxides usually being disposed upon a support, for example silica or alumina.

For example, U.S. Patent No. 4,209,656, issued September 15, 1981, and U.S. Patent No. 4,358,405, both to Hayes et al., describe a dehydration catalyst and process for making an alkyleneaziridine (such as ethylenimine) from an alkanolamine (such as monoethanolamine) ; the catalyst contains oxides of either tantalum or niobium together with the oxides of iron and chromium, in which the ratios of the metals are:

^M 10 ^Fβ 0.5-2.9 ^Cr 0.3-1.7 wherein M is tantalum or niobium.

U.S. Patent No. 4,301,036, issued November 17,

1981 to Childress et al., describes a dehydration catalyst for the dehydration of alkanolamines to alkyleneaziridines. This dehydration catalyst is prepared by applying a solution of a tungsten salt on to

a low surface area support (usually silicon carbide) , calcining the salt to tungsten oxide, and thereafter applying silica to the tungsten-coated support so as to form a coating of silica over the tungsten. U.S. Patent No. 4,337,175, issued June 29,

1982 to Ramirez, describes a dehydration catalyst for the dehydration of alkanolamines to alkyleneaziridines. This dehydration catalyst consists essentially of an oxide of tantalum or niobium with an alkaline earth metal oxide as a promoter on an inert support, for example a low surface area, high purity alumina. Other catalysts have been used for the production and conversion of monoalkanolamines. For example, U.S. Patent No. 4,524,143, issued June 18, 1985 to Vanderpool, describes a process for the production of linear polyethylenepolyamines from ethylenediamine and monoethanolamine using thermally activated pelleted catalyst compositions comprising zirconium silicate having phosphorus deposited thereon. Also, U.S. Patent No. 4,438,281, issued March

20, 1984 to Johnson, describes the selective production of monoalkanolamines from alkylene oxides and ammonia over acidic inorganic catalysts, such as acidic silica-aluminas, natural zeolites and acid clays. It has now been discovered that 3-hydroxyalkylamines can be converted to the

corresponding aziridines using as catalysts molecular sieves loaded with certain metals. Summary of the Invention

This invention provides a process for the dehydration of a £-hydroxyalkylamine to the corresponding aziridine, which process comprises contacting the amine with a molecular sieve, the molecular sieve having incorporated therein at least one metal selected from the group consisting of the alkali metals and the alkaline earth metals, the contacting of the amine with the molecular sieve being effected under conditions effective to convert the amine into the corresponding aziridine. Detailed Description of the Invention The molecular sieves used in the process of the present invention can be chosen from any of the known classes of molecular sieves. Thus, for example, the molecular sieve may be a natural or synthetic zeolite aluminosilicate, or a microporous form of silica, such as Silicalite (described in U.S. Patent No. 4,061,724 issued December 6, 1977 to R.W. ^" Grose et al) . The molecular sieve may also be a non-zeolitic molecular sieve of the aluminophosphate or silicoaluminophosphate type. Such non-zeolitic molecular sieves comprise a large number of aluminophosphates and silicoaluminophosphates having a variety of crystal

structures, which may include one or more other elements in addition to aluminum, phosphorus and silicon. Since many of the non-zeolitic molecular sieves are not described in U.S. Patents, and some are not described in publically-available literature, much material describing these non-zeolitic molecular sieve has to be repeated herein. However, for the convenience of the reader, the manner in which the non-zeolitic and other molecular sieves are used in the process of the present invention will first be described, and thereafter the chemical nature, and methods for the preparation, of the non-zeolitic molecular sieves will be described.

PROCESS OF THE INVENTION As already mentioned, in the process of the present invention an 0-hydroxyalkylamine is contacted with a molecular sieve to produce the corresponding aziridine. The process of the present invention is especially useful for the conversion of monoethanolamine to ethylenimine, but may also be used for other production of other substituted aziridines, for example propylenimine (2-methylaziridine) from propanolamine (/3-hydroxypropylamine) .

When the molecular sieve used in the process of the present invention is a zeolite, it may be any of the natural αr synthetic zeolites known in the art.

Such zeolites include, for example, zeolite X, zeolite Y

— o*

(see U.S. Patent No. 3,130,007), steam-stabilized zeolite Y (ultra-stable Y) , zeolite β (see U.S. Patent No. 3.308,069), zeolite KZ-2 ^' 0 (see U.S.' Patent No. 3,445,727), faujasite, erionite, mordenite, offretite, chabazite, LZ-10 (see U.K. Patent No. 2,014,970), LZ-210 (see U.S. Patent No. 4,503,023 to Breck) , FU-1-type zeolites, NU-type zeolites, and the ZSM zeolites denominated by the nomenclature "ZSM-n" where "n" is an integer. ZSM zeolites include but are not limited to ZSM-3 (see U.S. Patent No. 3,415,736), ZSM-5 (see U.S. Patent No. 3,702,886 and Reissue No. 29,948), ZSM-11 (see U.S. Patent No. 3,709,979), ZSM-12 (see U.S. Patent No. 3,832,449), ZSM-23 (see U.S. Patent No. 4,076,842), ZSM-35 (see U.S. Patent No. 4,016,245), ZSM-38 (see U.S. Patent No. 4,046,859) and ZSM-48 (see U.S. Patent No.

4,423,021). A particularly preferred zeolite for use in the process of the present invention is LZ-105, manufactured by Union Carbide Corporation; this zeolite is described and claimed in U.S. Patent No. 4,257,885. As already mentioned, the aluminophosphate or silicoaluminophosphate molecular sieves useful in the process of the present invention are described in detail below. However, at this point it is noted that the preferred aluminophosphate molecular sieves are the AlP0 ₄ 's described and claimed in U.S. Patent 4,310,440, issued January 12, 1982 to Wilson et al. Illustrative

AIPO ₄ species are AlP0 ₄ -5 and A1P0 ₄ -11, the latter being preferred.

The preferred silicoaluminophosphate molecular sieves for use in the process of the present invention are the SAPO's described and claimed in U.S. Patent 4,440,871 issued April _, 23, 1984 to Lok et al. Illustrative SAPO species are SAPO-5, SAPO-11 and SAPO-34.

In their as-synthesized form, the non-zeolitic molecular sieves (and some of the other molecular sieves) contain within their internal pore systems at least one form of the organic te plating agents used in their synthesis. The organic moiety may be present, at least in part, as a charge-balancing cation, and indeed this is generally the case with as-synthesized aluminosilicate zeolites prepared from organic-containing reaction systems. It is possible, however, that some or all of the organic moiety is an occluded molecular species in a particular species of molecular sieve. Such templating agents within the pore system may interfere with the catalytic activity and incorporation of metals into the molecular sieve and accordingly the templating agents should be removed before metal is incorporated into the molecular sieve or the molecular sieve is used as ^' a catalyst. As a general rule the templating agent, and hence the occluded

organic species, is too large to move freely through the pore system of the molecular sieve and must be removed by calcining the molecular sieve at temperatures of 200° to 700 ^β C, preferably about 350° to about 600 ^β C, to thermally degrade the organic species. In a few instances the pores of the molecular sieve are sufficiently large to permit transport of the templating agent, particularly if the latter is a small molecule, and accordingly complete or partial removal thereof can be accomplished by conventional desorption procedures, such as solvent extraction, which will be familiar to those skilled in the molecular sieve art.

Before being used in the process of the present invention, the molecular sieve is loaded with (i.e., has incorporated therein) at least one metal selected from the group consisting of the alkali metals and the alkaline earth metals. Of these metals, the alkali metals are preferred, with cesium being the especially preferred metal. Desirably, the amount of metal incorporated into the molecular sieve is up to about 20 weight percent of the weight of the molecular sieve (as measured prior to incorporation of the metal therein) .

The incorporation of the metal into the molecular sieve may be effected by any of the techniques well-known to those skilled in the molecular sieve art

for loading metals into the pores of molecular sieves; the preferred technique for metal incorporation depends upon the type of molecular sieve used. In the case of those molecular sieves having a significant ion-change capacity, such as zeolites, silicoaluminophosphates and aluminophosphates containing at least one framework element in addition to aluminum and phosphorus, the metal is desirably incorporated by ion-exchange; appropriate techniques for such ion-exchange are well- known to those skilled in the molecular sieve art.

Following the ion-exchange, the catalyst may be washed, but such washing is not recommended since in some cases it has been found to lower the selectivity of the catalyst to the desired aziridine. In the case of those molecular sieves not having a significant ion-change capacity, such as the AIPO4 aluminophosphates and silica molecular sieves, the metal is desirably incorporated into the molecular sieve by contacting the molecular sieve with a solution of a salt of the metal under conditions allowing the solution to penetrate the pores of the molecular sieve, and thereafter drying the molecular sieve to drive off the solvent from the catalyst. To facilitate the entry of the solution into the pores of the molecular sieve, the molecular sieve is preferably degassed prior to being contacted with the solution of the metal salt. The

solution is conveniently introduced into the molecular sieve by the so-called "incipient wetness" technique; in this technique, the pore volume of the molecular sieve is determined and the volume of the solution of the metal added to the molecular sieve (preferably after degassing of the molecular sieve) is adjusted to substantially equal this pore volume; this technique enables the amount of metal added to the molecular sieve to be controlled accurately. Following the addition of the metal, the molecular sieve is normally dried and then calcined to convert the metals to their oxides. When loading the metal into the molecular sieve by ion-exchange, incipient wetness or other technique, the nature of the metal compound used is not critical; in general any sufficiently soluble compound of the relevant metal may be employed, provided of course that the compound does not leave in the molecular sieve residues which interfere with the desired catalytic activity. It has been found that acetates and nitrates are often useful for introducing the metal into the molecular sieve.

The process of the present invention may be conducted with the amine in the ^" liquid phase. However, in view of the temperatures which are needed in practice to carry out the process of the present invention at an economical rate, it is preferred that the process of the

present invention be operated as a heterogeneous, gas phase reaction with the amine in the gaseous phase, since a gas phase process can be run at higher temperatures under relatively moderate pressures (typically of the order of a few atmospheres) using comparatively inexpensive equipment.

In .such a gas phase process, the amine may be mixed with an inert (i.e., such that it does not interfere with the course of the amine-aziridine reaction) carrier gas, (such as nitrogen or ammonia) while being contacted with the molecular sieve, although the use of such an inert carrier gas is not essential in the process of the present invention, which can be operated using pure amine as the gaseous feed. The degree of dilution of the amine with such an inert carrier gas may vary considerably depending upon any process constraints restricting the use of inert diluents. (For example, in commercial production, the use of very large quantities of inert carrier gas is disadvantageous due to the cost of pumping large volumes of gas and increased difficulty in isolating the product, which increase the energy costs of the process.) If the process of the present invention is to be carried out using an inert gas, in general it is recommended that the amine constitute from about 1 to about 90, and preferably about 9 to about 30, mole

percent of the amine/inert gas feed. Increasing the dilution of the amine tends to increase the selectivity of the reaction to the desired aziridine, but at the cost of reduced conversion. Selection of the temperature at which the process of the present invention is to be conducted involves a compromise between selectivity to the desired aziridine product and conversion of the amine used as starting material. It is recommended that the process of the present invention be conducted at a temperature in the range ^' of about 250*C to about 500*C; below this temperature range, the reaction tends to proceed too slowly, while at very high temperatures, the selectivity to the desired aziridine product decreases dramatically. At least for ethylenimine production, the preferred temperature range is from about 350"C to about 425"C. The process of the present invention can be run over a wide range of pressures ranging from sub-atmospheric pressures to 1000 psig. (6.9 MPa.) or more. However, since the use of very high pressures does not confer any significant advantages but increases equipment costs, it is recommended that the process of the present invention be carried out at a pressure of from about atmospheric pressure to about 100 psig. (about 0.7 MPa.) .

— . - ^* —

The process of the present invention can also be carried out over a wide range of weight hourly space velocities of the amine. For example, weight hourly space velocities of from about 0.1 to about 50 may be employed, with the preferred range of weight hourly space velocity being from about 0.5 to about 10, based on the amine.

The ^' molecular sieve catalysts used in the process of the present invention enable the amine-aziridine reaction to be carried out at high selectivities. As illustrated in the Examples below, the process of the present invention can be carried out with a selectivity to the aziridine of at least about 50%. As with some reactions catalyzed by molecular sieves, the conversion achieved in the process of the present invention may fall as the time for which the molecular sieve catalyst has been used in the process increases. If the molecular sieve catalysts become deactivated, then the deactivated catalyst can readily be regenerated by heating in air at an appropriate temperature (typically about 500 ^β C) and for an appropriate period (typically one hour) .

The molecular sieve may be modified by depositing or impregnating the molecular sieve with cations, anions or salts (other than the alkali metal or

alkaline earth metal_ used to render the molecular sieve efficacious in the process ^' of the present invention) so as to improve its efficacy ^' as a catalyst in the process .of the present- invention. Technique ^' s which may be ^" employed to effect the deposition or impregnation of a molecular sieve are generally known in the art. Such procedures may involve such procedures as (1) impregnating the molecular sieve with a solution comprising a solvent or solubilizing agent of one or more such modifying materials in an amount sufficient to deposit the desired weight of such materials in the molecular sieve and/or (2) exchanging the molecular sieve with a solution containing the modifying material. The impregnation or deposition of the modifying materials may generally be accomplished by heating the molecular sieve at an elevated temperature to evaporate any liquid present to effect deposition or impregnation of the modifying material on to the interior and/or exterior surface of the molecular sieve, or by the exchange of cations present in the molecular sieve with cations that provide for the desired properties (provided of course that the molecular sieve is one having a significant ion-exchange capacity) . Alternatively, the modifying material may be formed on the molecular sieve from a solution, an emulsion or a slurry containing the modifying material _*

Impregnation or exchange procedures are generally the preferred techniques because they - utilize and introduce the modifying material more efficiently than other procedures such as coating procedures since a coating procedure is generally not able to effect substantial introduction of the modifying material on-to the interior surfaces of the molecular sieve. In addition, coated materials are more generally susceptible to the loss of the modifying materials by abrasion.

Suitable modifying materials include transition metals and the salts thereof including inorganic ^' and organic salts such as nitrates, halides, hydroxides, sulfates and carboxylates. Other modifying materials generally employed in the art are also believed to be employable in the molecular sieves.

In carrying out the process of the present invention, the molecular sieves may be admixed (blended) or provided sequentially to other materials which may provide some property which is beneficial under process conditions, such as improved temperature resistance or improved catalyst life by minimization of coking, or which are simply inert under the process conditions used. Such materials may include synthetic or naturally-occurring substances as well as inorganic materials such as clays, silicas, aluminas, metal oxides

and mixtures thereof. In addition, the molecular sieves may be formed with materials such as silica, alumina, silica-alumina, silica-magnesia, silica-zirconia, sil ^' ica-thoria, silica-berylia, and silica-titania, as well as ternary compositions, such as silica-alumina- thoria, silica-alumina-zirconia and clays present as binders. The relative proportions of the above materials and the molecular sieves may vary widely with the molecular sieve content ranging between about 1 and about 99 percent by weight of the composite.

The following Examples are provided to further illustrate the process of the present invention, but are not limitative thereof. Unless otherwise specified, all parts, proportions etc. are by weight. EXAMPLES

The following Examples illustrate the use of cesium-loaded AIPO4-II and LZ-105 in the process of the present invention. The characteristic X-ray table for

AIPO ₄ -II is given in U.S. Patent No. 4,310,440 at Table 8 in column 15, but is repeated below for convenience.

&lP0 ₄ rll

Relative 2Θ d(A) Intensity 100 x I/I _r

Experimental Conditions

The various molecular sieve catalysts were prepared as described below, calcined in air following -synthesis to remove the organic templating agent, and then calcined for one hour under nitrogen at the reaction temperature prior to use. Between each run, the catalysts' were regenerated by calcination at 500"C in air for l to 12 hours.

The experiments were conducted using a micro reactor consisting of a 3/8 inch (9 mm.) diameter stainless steel tube encased in a 1 inch (25 mm.) diameter sheath of stainless steel heated with an electric split furnace. Approximately 1 gram of catalyst as the powder was dispersed among about 5 grams of 20-30 U. S. mesh quartz chips and placed.in the heated zone of the reactor. The reactor tube was disposed vertically with a downward flow of reactants and products. Connected to the inlet of the reactor were a source of nitrogen carrier gas and a liquid feed line containing monoethanolamine connected to a high pressure liquid chromatography (HPLC) type solvent pump. Immediately below the reactor was disposed a cold trap kept at 0*C. Gas chromatographic analysis of the outlet gas indicated that all of the ethylenimine produced was- retained in the cold trap and only very small amounts of ammonia and a material with a retention time similar to

that of ethylene passed the trap. The products of the reaction collected in the cold trap were analyzed by gas chromatography on a 12 foot by 1/8 inch (3658 by 3 mm.) column containing TERGITOL non-ionic TMN (a polyether liquid phase) and 3 percent sodium methylate on 60/80

Chromasorb W-NAW, or on a 10 foot by 1/8 inch (3048 by 3 mm.) column containing 8 percent TERGITOL non-ionic E68 and 2 percent potassium hydroxide.

Example 1 A sample of A1P0 ₄ -11 was loaded with 20 percent of its own weight of cesium acetate by the incipient wetness technique described above; thus, the concentration of cesium in the metal-loaded catalyst was approximately 0.104 moles per 100 grams of AIPO ₄ -II prior to metal loading. The reactor was charged with 1.0 g. of the cesium-loaded catalyst and heated to 375 ^β C. Nitrogen carrier gas was passed through the reactor at a rate of 20 ml/ in. at atmospheric pressure, and liquid monoethanolamine was fed into the nitrogen stream at a rate of 8 ml/hour. Analysis of the products of the reaction showed that more than 70 percent of the products were ethylenimine, and that this aziridine was formed at a rate of approximately 3 lb/hour/ft ³ , of catalyst (approximately 48 kg/hour/m ³ . of catalyst).

-19- Examole 2 LZ-105 zeolite was ion-exchanged with a solution of cesium acetate until the ion-exchange was total. The ion-exchanged zeolite was not washed. The reactor was charged with 1.0 g. of the cesium-loaded catalyst and heated to 375"C. Nitrogen carrier gas was passed through the reactor at a rate of 20 ml/min. at atmospheric pressure, and liquid monoethanolamine was fed into the nitrogen stream at a rate of 0.6 ml/hour. Analysis of the products of the reaction during the first hour of operation of the catalyst showed that about 50-60 percent of the products were ethylenimine, and that this aziridine was formed at a rate of approximately 10 lb/hour/ft ³ . of catalyst (approximately 160 kg/hour/m ³ . of catalyst). As the operating time of the catalyst increased, the selectivity to ethylenimine decreased and eventually morpholine became the major product.

Example 3 Samples of AIPO4-II was loaded with 20 percent of their own weight of cesium acetate or cesium nitrate by the incipient wetness technique described above; the samples were refluxed for 3 hours with 0.5M solutions of the cesium salt, then filtered, the salt solution treatment was repeated, the product re-filtered and the solids dried in an oven overnight at 110 ^β C.

Runs were conducted at varying temperatures and monoethanolamine and nitrogen flow rates, as set forth in Table 1 below. The conversions and selectivities to ethylenimine achieved are shown in Table 1.

Table 1

N flow rate MEA flew rate Conversion Selectivit

Attention is directed to the co-pending application of Kurt D. Olson and Steven W. Kaiser, of even date herewith (Applicant's reference D-14643) , which describes and claims a process for the catalytic dehydration and/or deamination of alkanolamines, including monoethanolamine, to give mixtures of alkanolamines, alkylamines and (in some cases) aziridines, including ethylenimine. The catalyst used is a non-zeolitic molecular sieve, which is not metal-loaded.

NON-ZEOLITIC MOLECULAR SIEVES The term "non-zeolitic molecular sieves" or "NZMS" is defined in the instant invention to include the "SAPO ¹ . ¹ molecular sieves of U.S. _. Patent No. 4,440,871 and U.S. Serial No. 575,745, filed January 31, 1984, "ELAPSO" molecular sieves as disclosed in U.S. Serial No. 600,312, filed April 13, 1984, and certain "A1PO ", "MeAPO", "FeAPO", "TAPO" and "ELAPO" molecular sieves, as hereinafter described. Crystalline "A1PO " aluminophosphates are disclosed in U.S. Patent No.

4,310,440 issued January 12, 1982, and in U.S. Serial No. 880,559, filed June 30, 1986; crystalline metal aluminophosphates (MeAPOs where "Me" is at least one of Mg, Mn, Co and Zn) are disclosed in U.S. Patent No. 4,567,029, issued January 28, 1986; crystalline ferroaluminophosphates (FeAPOs) are disclosed in U.S. Patent No. 4,554,143, issued November 19, 1985; titanium aluminophosphates (TAPOs) are disclosed in U.S. Patent No. 4,500,651, issued February 19, 1985; certain non-zeolitic molecular sieves ("ELAPO") are disclosed in EPC Patent Application 85104386.9 (Publication No. 0158976, published October 13, 1985) and 85104388.5 (Publication No. 158349, published October 16, 1985) ; and ELAPSO molecular sieves are disclosed in copending U.S. Serial No. 600,312, filed April 13, 1984 (EPC

Publication No. 0159624, published October 30, 1985).

The aforementioned applications and patents are incorporated herein by reference thereto. The nomenclature employed herein to refer to the members of the aforementioned NZMSs is consistent with that employed in the aforementioned applications or patents. A particular member of a class is generally referred to as a "-n" species wherein "n" is an integer, e.g., SAPO-11, MeAPO-11 and ELAPSO-31. ^* In the following discussion on NZMSs set forth hereinafter the mole fraction of the NZMSs are defined as compositional values which are plotted in phase diagrams in each of the identified patents, published applications or copending applications.

ELAPSO MOLECULAR SIEVES "ELAPSO" molecular sieves are described in copending U.S. Serial No. 600,312, filed April 13, 1984, (EPC Publication No. 0159,624, published October 30, 1985, incorporated herein by reference) as crystalline molecular sieves having three-dimensional microporous framework structures of EL0-, A10-, -PO _? ' ^s ^° ₂ ^ox *-** ^cie units and having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (EL _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

0.3; "EL" represents at least one element capable of forming a three dimensional oxide framework, "EL" being characterized as an element having a mean "τ-0" distance in tetrahedral oxide structures between about 1.51 Angstroms and about 2.06 Angstroms, "EL" having a cation electronegativity between about 125 kcal/g-atom to about 310 kcal/gm-atom and "EL" being capable of forming stable M-O-P, M-O-Al or M-O-M bonds in crystalline three dimensional oxide structures having a "M-O" bond dissociation energy greater than about 59 kcal/g-atom at 298*K; and "w", "x", "y" and "z" represent the mole fractions of "EL", aluminum, phosphorus and silicon, respectively, present as framework oxides, said mole fractions being within the limiting compositional values or points as follows:

Mole Fraction y ( z + w)

0.39-(0.01)p 0.01(p + 1) 0.60 0.01(p + 1) 0.60 0.39

0.01 0.98 0.01 0.39 where "p" is an integer corresponding to the number of elements "El" in the (El Al P Si_)0, constituent. The "ELAPSO" molecular sieves ^' are also described as crystalline molecular sieves having

three-dimensional icroporous framework structures of

EL0_, AIO,, Si0 ₂ and P0 ₂ tetrahedral oxide units and having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (EL _w Al _χ P _y Si _z )0 ₂ wherein "R" represents at least one organic templating agent present- in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(ELwAlxPy,Siz)02« and has a value of from zero to about 0.3; "EL" represents at least one element capable of forming a framework tetrahedral oxide and is selected from the group consisting of arsenic, beryllium, boron, chromium, cobalt, gallium, germanium, iron, lithium, magnesium, manganese, titanium and zinc; and "w", "x", "y" and "z" represent the mole fractions of "EL", aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides, said mole fractions being within the limiting compositional values or points as follows:

Mole Fraction fz - w)

0.39-(0.01)p 0.01(p + 1) 0.60 0.01(p + 1) 0.55 0.35 0.10 0.35 where "p" is as above defined.

The "ELAPSO" molecular sieves include numerous species which are intended herein to be within the scope of the term "non-zeolitic molecular sieves" such being disclosed in the following copending and commonly assigned applications, incorporated herein by reference thereto [ (A) following a serial number indicates that the application is abandoned, while (CIP) following a serial number indicates that the application is a continuation-in-part. of the immediately preceding application and (C) indicates that the application is a continuation of the immediately preceding application] :

TiAPSO MOLECULAR SIEVES

The TiAPSO molecular sieves of U.S. Serial

No. 600,179, filed April 13, 1984 (now U.S. Patent No.

4,684,617), and U.S. Serial No. 49,274, filed May 13, 1987, have three-dimensional icroporous framework structures of i0 ₂ , AIO ~, PO + and SiO. tetrahedral oxide units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Ti _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(TiwAlxPySiz)02- and has a value of from zero to about

0.3; and "w", "x", "y" and "z" represent the mole fractions of titanium, aluminum, phosphorus .and silicon, respectively, present as tetrahedral oxides and each has a value of at least 0.01. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows: Mole Fraction

Point 5£ Y ( z + w)

A 0.60 0.38 0.02

B 0.38 0.60 0.02

C 0.01 0.60 0.39 D 0.01 0.01 0.98

E 0.60 0.01 0.39

In a subclass of TiAPSO molecular sieves the values "w", "x". "y" and "z" in the above formula are within the tetragonal compositional.area defined by points a, b, c and d, said points a, b, c and d representing the following values for "w", "x", "y" and ^» z":

Point a b c d

TiAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing active sources of titanium, silicon, aluminum and phosphorus, and preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between 50 ^β C and 250*C, and preferably between 100'C ^' and 200°C until crystals of the TiAPSO product are obtained, usually a period of from hours to several weeks. Generally, the

crystallization time is from about 2 hours to about 30 days and typically from about 4 hours to about 20 days. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the TiAPSOs, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Ti _w Al _χ P _y Si ₂ )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300; and "w", "x", "y" and "z" represent the mole fractions of.titanium, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point F G H I J

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and *-z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing titanium, aluminum, phosphorus and silicon as framework tetrahedral oxides are prepared as follows:

Preparative Reaσents TiAPSO compositions are typically.prepared using numerous regents. Typical reagents which may be employed and abbreviations employed in U.S. Serial No. 600,179 for such reagents are as follows:

(a) Alipro: aluminum isopropoxide; (b) LUDOX-LS: LUDOX-LS is the tradename of

DuPont for an aqueous solution of 30 weight percent SiO_ and 0.1 weight percent Na_0;

(c) H.PO.: 85 ^* weight percent aqueous phosphoric acid;

(d) Tiipro: titanium isopropoxide;

(e) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxid ;

(f) Pr ₂ NH: di-n-propylamine, (C ₃ H _? ) NH; (g) Pr ₃ NH: tri-n-propylamine, (C-H-J-N;

(h) Quin: Quinuclidine, (C-H.-N) ;

(i) MQuin: Methyl Quinuclidine hydroxide,

(C _? H ₁₃ NCH ₃ OH) ; and (j) C-hex: cyclohexylamine. Preparative Procedures

TiAPSOs may be prepared by forming a starting reaction mixture by adding the H.PO. and the water. This mixture is mixed and to this mixture aluminum isopropoxide is added. This mixture is then blended until a homogeneous mixture is observed. To this mixture the LUDOX-LS is added and the resulting mixture blended (about 2 minutes) until a homogeneous mixture is observed.

The titanium isopropoxide is added to the above mixture and the resulting mixture blended until a homogeneous mixture is observed. The organic templating agent is then added to the resulting mixture and the resulting mixture blended until a homogeneous mixture is observed, i.e., about 2 to 4 minutes. When the organic templating agent is quinuclidine the procedure is modified such that the quinuclidine is dissolved in

about one half the water and accordingly the H.PO. is mixed with about one half the water. (The pH of the . mixture is measured and adjusted for temperature) . The mixture is then placed in a lined (polytetrafluoro- ethylene) lined stainless steel pressure vessel and digested at a temperature (150 ^β C or 200*C) for a time or placed in lined screw top bottles for digestion at 100 ^* C. Digestions are typically carried out under autogenous pressure. The products are removed from the reaction vessel and cooled.

MσAPSO MOLECULAR SIEVES The MgAPSO molecular sieves of U.S. Serial

No. 600,180, filed April 13, 1984 have three-dimensional microporous framework structures of MgO_ 2-, -A10--, PO,'T¬

and SiO, tetrahedral oxide units and have an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Mg _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(M',wAl,xPySiz„)0.2 and has a value from zero (0) to about

0.3; and "w", "x", "y" and "z" represent the mole fractions of magnesium, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides and

each preferably has a value of at least 0.01. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Fraction Point A B C D E

In a preferred subclass of the MgAPSO molecular sieves the values "w", "x", "y" and "z" in the above formula are within the limiting compositional values or points as follows:

Mole Fraction y ( z + w)

0.43 0.02

0.55 0.02 0.55 0.35 0.10 0.35

MgAPSO compositions are generally synthesized by hydrothermal crystallization for an effective time at effective pressures and temperatures from a reaction ^• mixture containing reactive sources of magnesium, silicon, aluminum and phosphorus, an organic templating,

i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and may be an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetra- fluoroethylene and heated, preferably under autogenous pressure at a temperature between 50*C and 250"C, and preferably between 100 ^* c and 200*C until crystals of the MgAPSO product are obtained, usually a period of from several hours to several weeks.' Generally, the crystallization period will be from about 2 hours to about 30 days with it typically being from about 4 hours to about 20 days for obtaining MgAPSO crystals. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the MgAPSO compositions, it is preferred to employ reaction mixture compositions expressed in terms of the molar ratios as follows: aR : (M- _w Al _χ P _y Si ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and can have a value within the range of from zero (0) to about 6 and is more preferably an effective amount greater than zero to about 6; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300; and "w", "x", "y" and "z" represent the mole fractions of

agnesium, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01. In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

M e F ac

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing magnesium, aluminum, phosphorus and silicon as framework tetrahedral oxides are prepared as follows: Preparative Reaσents

MgAPSO compositions are prepared using numerous reagents. Typical reagents which may be employed to prepare MgAPSOs include:

(a) Alipro: aluminum isopropoxide; (b) CATAPAL: Trademark of Condea for hydrated pseudoboehmite;

(c) LUDOX-LS: ^" Trademark of DuPont for an aqueous solution of 30 weight percent SiO, and 0.1 weight percent Na_0; (d) Mg(Ac)_: magnesium acetate tetrahydrate, Mg(C ₂ H ₃ 0 ₂ ) .4H ₂ 0; (e) ^' H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid in water;

(f) TBAOH: tetrabutylammonium hydroxide (40 wt. % in water) ;

(g) Pr«NH: di-n-propylamine; (h) Pr.NH: tri-n-propylamine; (i) Quin: Quinuclidine;

(j) MQuin: Methyl Quinuclidine hydroxide, (17.9% in water) ;

(k) C-hex: cyclohexylamine;

(1) TEAOH: tetraethylammonium hydroxide (40 wt. % in water) ;

( ) DEEA: Diethylethanolamine; (n) i-Pr ₂ NH: di-isopropylamine;

(o) TEABr: tetraethylammonium bromide; and

(p) TPAOH: tetrapropylammonium hydroxide (40 wt. % in water) .

Preparative Procedures The MgAPSO compositions may be prepared by preparing reaction mixtures having a molar composition expressed as: eR:fMgO:hAl ₂ 0 ₃ :iP ₂ 0 ₅ :gSi0 ₂ :jH ₂ 0 wherein e, f, g, h, i and j represent the moles of template R, magnesium (expressed as the oxide), SiO_, A1 ₂ 0 ₃ , P ₂ °5 ( ^H 3 ^P expressed as P ₂ ° ₅ ) an H ₂ 0, respectively. The reaction mixtures may be prepared by the following representative procedures, designated hereinafter as Methods A, B and C.

Method A The reaction mixture is prepared by mixing the ground aluminum source (Alipro or CATAPAL) with the H-PO. and water on a gradual basis with occasional cooling with an ice bath. The resulting mixture is blended until a homogeneous mixture is observed. When the aluminum source is CATAPAL the water and H 3,PO4. are first mixed with the CATAPAL added thereto. The magnesium acetate is dissolved in a portion of the water and is then added followed by addition of the LUDOX-LS. The combined mixture is blended until a homogeneous mixture is observed. The organic templating agent is added to this mixture and blended until a homogeneous mixture is observed. The resulting mixture (final

reaction mixture) is placed in ^" a lined (pclytetrafluoro- ethylene) stainless steel pressure vessel and digested at a temperature (150"C or 200"C) for an effective time. Alternatively, if the digestion temperature is 100 ^β C the final reaction mixture is placed in a lined

(polytetrafluoroethylene) screw top bottle for a time. Digestions are typically carried out under autogenous pressure. The products are removed from the reaction vessel, cooled and evaluated as set forth hereinafter. Method B

When method B is employed the organic templating agent is di-n-propylamine. The aluminum source, silicon source and one-half of the water are first mixed and blended until a homogeneous mixture is observed. A second solution was prepared by mixing the remaining water, the H ₃ PO. and the magnesium acetate. This solution is then added to the above mixture. The magnesium acetate and H ₃ PO. solution is then added to the above mixture and blended until a homogeneous mixture is observed. The organic templating agent(s) is/are then added and the resulting reaction mixture digested and product recovered as in Method A.

Method C Method C is carried out by mixing aluminum isopropoxide, LUDOX LS and water in a blender or by mixing water and aluminum iso-propoxide in a blender

folϊowed ^' by ^■ - addition of the LUDOX LS. H_3PO4„ and ^' magnesium acetate are then added to this mixture. The organic templating agent is then added to the resulting mixture and digested and product recovered as in Method A.

MnAPSO MOLECULAR SIEVES The MnAPSO molecular sieves of U.S. Serial No. 600,175, filed April 13, 1984 (now U.S. Patent No.

4,686,092 issued August 11, 1987), have a framework structure of MnO_ -2, A10 -, PO.+ and SiO- tetrahedral units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Mn _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intraerystalline pore system; "m" represents the molar amount of "R" present per mole of

(MnwAlxPySiz)02_ and has a value of zero to about 0.3; and "w", "x", "y" and "z" represent the mole fractions of the elements manganese, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

MnAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of manganese, silicon, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel,. preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50"C and about 250 ^* C, and preferably

between about 100°C and about 200°C until crystals of the MnAPSO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 20 days, have been observed. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the MnAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Mn _w Al _χ P _y Si _z )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300; and "w", "x", "y" and "z" represent the mole fractions of manganese, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point

G H

I

J

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing manganese, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows: Preparative Reagents

MnAPSO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare MnAPSOs include:

(a) Alipro: aluminum isopropoxide; (b) CATAPAL: Trademark of Condea Corporation for hydrated pseudoboehmite; (c) LUDOX-LS: LUDOX-LS is the tradename of DuPont for an aqueous solution of 30 weight percent SiO_ and 0.1 weight percent Na ₂ 0;

(d) H-PO : 85 weight percent aqueous phosphoric acid;

(e) MnAc: Manganese acetate,

^Mn < ^C 2 ^H 3°2>2. ^4H 2° ^? . (f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(g) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(h) Pr ₂ NH: di-n-propylamine, (C ₃ H_) ₂ NH; (i) Pr ₃ N: tri-n-propylamine, (C ₃ H_) ₃ N;

(j) Quin: Quinuclidine, (C ₇ H_ ₃ N) ;

(k) MQuin: Methyl Quinuclidine hydroxide,

(C ₇ H ₁₃ NCH ₃ OH) ;

(1) C-hex: cyclohexylamine; (m) TMAOH: tetramethylammonium hydroxide;

(n) TPAOH: tetrapropylammonium hydroxide; and

(o) DEEA: 2-diethylaminoethanol.

Preparative Procedures

MnAPSOs are prepared by forming a starting reaction mixture by adding the H ₃ PO to one half of the quantity of water. This mixture is mixed and to this mixture the aluminum isopropoxide or CATAPAL is added.

This mixture is then blended until a homogeneous mixture is observed. To this mixture the LUDOX LS is added and the resulting mixture blended (about 2 minutes) until a homogeneous mixture is observed. A second mixture is

prepared using the manganese acetate and the remainder (about 50%) of the water. The two mixtures are admixed and the resulting mixture blended until a homogeneous mixture is observed. The organic templating agent is then added to the resulting mixture and the resulting mixture blended until a homogeneous mixture is observed, i.e., about 2 to 4 minutes. (The pH of the mixture is measured and adjusted for temperature) . The mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150'C or 200 ^β C) for a time or placed in lined screw top bottles for digestion at 100 ^β C. Digestions are typically carried out at the autogenous pressure. CoAPSO MOLECULAR SIEVES

The CoAPSO molecular sieves of U.S. Serial No.

600,174, filed April 13, 1984 have three-dimensional microporous framework structures of Co0_ 2-, A10_—, P0_+

and SiO. tetrahedral units and have an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Co _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(CowAlxPySiz)02_ and has a value of from zero to about

0.3; and "w", "x", "y" and "z" represent the mole fractions of cobalt, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides, where the mole fractions "w", "x", "y" and "z" are each at least 0.01 and are generally defined, as being within the limiting compositional values or points as follows:

Mole Point A B C D E

In a preferred subclass of the CoAPSO molecular sieves the values of "w", "x", "y", and ^~~ z ^'~ in the above formula are within the limiting compositional values or points as follows:

Mole Fraction

Point x y. a 0.55 0.43 b 0.43 0.55 c 0.10 0.55 d 0.55 0.10

CoAPSO compositions are generally synthesized ^' by hydrothermal crystallization from a reaction mixture containing reactive sources of cobalt, silicon, aluminum

and phosphorus, an organic templating, i.e., structure- directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and optionally an alkali metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at an effective temperature which is generally between 50°C and 250"C and preferably between 100*C and 200'C until crystals of the CoAPSO product are obtained, usually for an effective time of from several hours to several weeks. Generally the effective crystallization time will be from about 2 hours to about 30 days and typically from about 4 hours to about 20 days. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the CoAPSOs, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Co _w Al _χ P _y Si _z )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6; "b" has a value of from zero (0) to about 500, preferably between about 2 and 300; and "w", "x", "y"

and "z" represent the mole fractions of cobalt, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01. In a preferred embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Fract o

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing cobalt, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows:

Preparative Reaσents CoAPSO compositions may be prepared using numerous reagents. Reagents which may be employed to

< prepared CoAPSOs include:

(a) Alipro: aluminum isopropoxide;

(b) CATAPAL: Trademark of Condea Corporation ' for pseudoboehmite;

(c) ^" LUDOX-LS: Trademark of DuPont for an aqueous solution of 30 weight percent ^s *^° ^and °* ^{1 we} *ig-h percent Na.O;

(d) Co(Ac) ₂ : cobalt acetate, Co(C ₂ H ₃ 0 ₂ ) ₂ .4H ₂ 0;

(e) CoSO.: cobalt sulfate, (CoS0..7H ₂ 0) ;

(f) H ₃ P0.: 85 weight percent phosphoric acid in water;

(g) TBAOH: tetrabutylammonium hydroxide (25 wt % in methanol) ;

(h) Pr ₂ NH: di-n-propylamine, (C ₃ H_) ₂ NH;

(i) Pr ₃ N: tri-n-propylamine, (C ₃ H_) ₃ N; (j) Quin: Quinuclidine (C ₇ H- ₃ N)

(k) MQuin: Methyl Quinuclidine hydroxide, (C ₇ H ₁₃ NCH ₃ 0H) ;

(1) C-hex: cyclohexylamine;

(m) TEAOH: tetraethylammonium hydroxide (40 wt. % in water) ;

(n) DEEA: ^" diethanolamine;

(o) TPAOH: tetrapropylammonium hydroxide (40 wt. % in water) ; and

(p) TMAOH: tetramethylammonium hydroxide (40 wt. % in water) .

Preparative Procedure CoAPSO compositions may be prepared by preparing reaction mixtures having a molar composition expressed as: e :fCoO:hAl ₂ 0 ₃ :iP ₂ 0 ₅ :gSi0 ₂ :jH ₂ 0 wherein e, f, h, i, g and j represent the moles of template R, cobalt (expressed as the oxide), A1-0 m-i, P- 20D _C

(H ₃ P0 ₄ expressed as ? ₂ ⁰ ₅ - ' ^s ° ₂ ^{and H} ₂ ⁰ ' respectively. The reaction mixtures are prepared by forming a starting reaction mixture comprising the H_PO. and one half of the water. This mixture is stirred and the aluminum source (Alipro or CATAPAL) added. The resulting mixture is blended until a homogeneous mixture is observed. The LUDOX-LS is then added to the resulting mixture and the new mixture blended until a homogeneous mixture is observed. The cobalt source (e.g., Co(Ac) ₂ , Co(SO.) or mixtures thereof) is dissolved in the remaining water and combined with the first mixture. The combined mixture is blended until a homogeneous mixture is observed. The organic templating agent is added to this mixture and blended for about two to four minutes until a homogeneous mixture is observed. The resulting mixture (final reaction mixture) is placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150'C, 200*C or 225"C) for a time. Digestions are typically

carried out at the autogenous pressure. The products are removed from the reaction vessel and cooled.

ZnAPSO MOLECULAR SIEVES The ZnAPSO molecular sieves of U.S. Serial No. 600,170, filed April 13, 1984 comprise framework structures of Zn0 ₂ -2, A10 ₂ -, P0 ₂ + and Si0 ₂ tetrahedral units having -an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Zn _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(ZnwAlxPy.Siz)02_ and has a value of zero to about 0.3; and "w", "x", "y" and "z" represent the .mole fractions of zinc, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides and each has a value of at least 0.01. The mole fractions "w", "x", "y" and "z" are generally defined being within the limiting compositional values or points as follows: o e a t o

Point A B C D E

Iri a preferred subclass of ZnAPSO molecular sieves the values "w", "x", "y ^ι: and "z" in the above formula are within the limiting compositional values or points as follows:

ZnAPSO compositions are generally synthesized by hydrothermal crystallization at effective process conditions from a reaction mixture containing active sources of zinc, silicon, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element or Group VA of the Periodic Table, and/or optionally an alkali of other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure, at a temperature between 50 ^* C and 250*C, and preferably between 100 ' C and 200 ^β C until crystals of the ZnAPSO product are obtained, usually a period of from several hours to several weeks.

Generally the effective crystallization period is from

about 2 hours to about 30 days with typical periods of from about 4 hours to about ^* 20 days being employed to obtain ZnAPSO ^' roducts. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the ZnAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : ^" (2n _w Al _χ P _y Si ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6; "b" has a value of from zero (0) to about 500, more preferably between about 2 and about 300; and "w", "x", "y" and "z" represent the mole fractions of zinc, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01. In a preferred embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point F G ^' 5 H

I J

In the foregoing expression of the reaction composition, the reactants are normalized with respect 0 _. to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing zinc, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows: 5 Preparative Reaσents

ZnAPSO compositions are typically prepared using numerous reagents. Reagents which may be employed to prepare ZnAPSOs include:

(a) Alipro: aluminum isopropoxide; 0 - (b) LUDOX-LS: LUDOX-LS is the trade name of

DuPoπt for an aqueous solution of 30 weight percent Si0 ₂ and 0.1 weight percent a ₂ 0; (c) CATAPAL: Trademark of Condea Corporation 5 for hydrated pseudoboehmite;

(d) H..PO : 85 weight percent aqueous phosphoric acid;

(e) ZnAc: Zinc Acetate, Zn(C ₂ H ₃ 0 ₂ ) ₂ .4H ₂ 0;

(f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(g) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(h) TMAOH: Tetramethylammonium hydroxide pentahydrate, (CH ₃ ) NOH.5H ₂ O; (i) TPAOH: 40 weight percent aqueous solution of tetrapropylammonium hydroxide, (C ₃ H _? ) ₄ N0H; (j) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH; (k) Pr ₃ N: Tri-n-propylamine, (C ₃ H _? ) ₃ N; (1) Quin: Quinuclidine, (C ₇ H ₁₃ N) ;.

(m) C-hex: cyclohexylamine; and (n) DEEA: diethylethanolamine, (C ₂ H ₅ ) ₂ NC ₂ H ₅ OH.

Preparative Procedure ZnAPSO compositions are typically prepared by forming reaction mixtures having a molar composition expressed as: eR:fZnO:gAl ₂ 0 ₃ :hP ₂ 0_:isi0 ₂ :jH ₂ 0 wherein e, f, g, h, i and j represent the moles of template R, zinc (expressed as the oxide), Al ₂ 0 ₃ , I^C (H ₃ P0. expressed as ^{and H} 2 ⁰ ' respectively.

The reaction mixtures are generally prepared by forming a starting reaction mixture comprising the H-PO. and a portion of the water. This mixture is stirred and the aluminum source added. The resulting mixture is blended until a homogeneous mixture is observed. The LUDOX LS is then added to the resulting mixture and the new mixture blended until a homogeneous mixture is observed. The zinc source (zinc acetate) is dissolved in the remaining water and combined with the first mixture. The combined mixture is blended until a homogenous mixture is observed. The organic templating agent is added to this mixture and blended for about two to four minutes until a homogenous mixture is observed. The resulting mixture (final reaction mixture) is placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at an effective temperature for an effective time. Digestions are typically carried out under autogenous pressure. The products are removed from the reaction vessel and cooled. FeAPSO MOLECULAR SIEVES

The FeAPSO molecular sieves of U.S. Serial No. 600,173, filed April 13, 1984 (now U.S. Patent No. 4,683,217) have three-dimensional microporous crystal framework structures of Fe0 ₂ ^" , (and/or Fe0 ₂ ^" ) , A10 ₂ ~, ■ ^'P0 ₂ ^{+ nci s} ^°2 "tetrahedral oxide units and having a unit empirical formula, on an anhydrous basis, of:

mR : (Fe _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the moles of "R" present per mole of (Fe_wAlxPySi„z)02_ and has a value of from zero (0)' to about 0.3; the maximum value of "m" in each case depends upon the molecular dimensions of the templating agent and the available void volume of the pore system of the particular molecular sieve involved; and "w", "x", "y" and "z" represent the mole fractions of iron, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides, said mole fractions being such that they are within the limiting compositional values or points as follows:

Point

A

B

C D

E

The values of w, x, y arid z may be as follows:

Mole Fraction

The FeAPSOs of the instant invention are generally synthesized by hydrothermal crystallization from a reaction mixture comprising reactive sources of iron, aluminum, phosphorus and silicon, and preferably one or more organic templating agents. Optionally, alkali or other metal(s) may be present in the reaction mixture and may act as templating agents. The reaction mixture is generally placed in a pressure vessel, preferably lined with an inert plastic material, such as polytetrafluoroethylene, and heated, preferably under autogenous pressure, at an effective temperature which is generally between about 50*C and about 250*C, and preferably between about 100 ^β C and 200*C, until crystals of the FeAPSO product are obtained, usually a period of from several hours to several weeks. Molecular sieves containing iron, aluminum, phosphorus and silicon as framework tetrahedral oxide units are typically prepared as follows:

Preparative Reagents FeAPSO compositions may be prepared using numerous reagents. Reagents which may employed to prepare FeAPSOs include: (a) Alipro: aluminum isopropoxide,

Al(OCH(CH ₃ ) ₂ ) ₃ ; (b) LUDOX-LS: LUDOX-LS is the trademark of Du Pont for an aqueous solution of 30 weight percent Si0 ₂ and 0.1 weight percent Na ₂ 0; (c) CATAPAL: trademark for hydrated aluminum oxide containing about 75 wt. percent Al_0 ₃ (pseudoboehmite phase) and about 25 wt. percent water; (d) Fe(Ac) ₂ : Iron (II) acetate; (e) FeSO.: Iron (II) sulfate hexahydrate;

(f) H ₃ P0.: 85 weight percent phosphoric acid in water;

(g) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; (h) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (i) Pr ₂ NH: di-n-propylamine ((C ₃ H _y ) ₂ NH); (j) Pr ₃ N: tri-n-propylamine ((C ₃ H ₇ ) ₃ N); (k) Quinϊ Quinuclidine (C-H.-N) ; (1) MQuin: Methyl Quinuclidine hydroxide

(C ₇ H ₁₃ NCH ₃ OH) ;

(m) TMAOH: tetramethylammonium hydroxide . pentahydrate; and (o) C-hex: cyclohexylamine. Preparative Procedures a) Reaction mixtures to prepare FeAPSOs are typically prepared by grinding an aluminum isopropoxide in a blender followed by slowly adding a H_PO. solution with mixing. A solution/dispersion of iron acetate in water is added and then a silica (e.g., LUDOX-LS) is added. The organic templating agent is then added to this mixture, or in some cases one-half of this mixture, and the mixture blended to form a homogeneous mixture. For example, in one embodiment, the number of moles of each component in the reaction mixture is as follows: Component Moles 1 ₂ 0 ₃ 0.9

P ₂ 0 ₅ 0.9

SiO. 0.2

FeO* 0.2 TEAOH 1.0

H ₂ 0 50

* Iron (II) acetate reported as Iron (II) oxide.

The reaction mixture is sealed in a stainless steel pressure vessel lined with polytetrafluoroethylene and heated in an oven at a temperature, time and under autogenous pressure. The solid reaction product is

recovered by filtration, washed with water and dried at room temperature. b) In another embodiment, reaction mixtures are prepared by grinding the aluminum isopropoxide in a blender followed by addition of a solution/dispersion of iron(II) acetate. H ₃ PO. is added to this mixture and the resulting, mixture blended to form a homogeneous mixture. A silica ^' (e.g., LUDOX-LS) is added to this mixture except that in some instances the silica may be added with the H ₃ P0 ₄ . The resulting mixtures were blended until a homogeneous mixture is observed. Organic templating agent is added to each mixture and the resulting mixtures placed in a stainless steel pressure vessel lined with polytetrafluoroethylene and heated, washed and the product recovered. In this embodiment the number of moles of each component in the reaction mixture is as follows:

Component Moles

A1 ₂ 0 ₃ 0.9 P ₂ 0 ₅ 0.9

Si0 ₂ 0.2

FeO* 0.2

Template 1.0

H ₂ 0 50

* Iron(II) acetate reported as Iron(II) oxide.

OUINARY MOLECULAR SIEVES

The -QuinAPSO quinary molecular sieves of U.S. Serial Nos. 600,168 and 600,181, both filed April 13, 1984, have three-dimensional microporous framework .5 structures of M0 ₂ ⁿ , A10 ₂ "\ P0 ₂ ⁺ and Si0 ₂ tetrahedral units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (M _w Al _x P _y Si _z )0 ₂ wherein "R" represents at least one organic templating

10 agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of (M _w Al _x PySi ₂ )0 ₂ and has a value of from zero (0) to about 0.3; M represents at least two elements selected from the group consisting of arsenic, beryllium, boron,

15 chromium, cobalt, gallium, germanium, iron, lithium, magnesium, manganese, titanium, vanadium and zinc; and "w", "x", "y" and "z" represent the mole fractions of M, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. Preferably, M represents the

20. combination of cobalt and manganese. The mole fractions "w", "x", "y", and "z" are generally defined as being within the limiting compositional values or points as follows:

Point A B C D E

Preferably the mole fractions w, x, y and z will fall within the limiting compositional values or points as follows:

Point a b c d e f

QuinAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of the elements M, aluminum, phosphorus and silicon and preferably an organic templating agent, i.e., structure-directing, agent. The structure-directing agents are preferably a compound of an element of Group VA of the Periodic Table, and may be an alkali or other

etal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure and at typical effective temperatures between 50"C and 250*C, preferably between 100*C and 200°C, until crystals of the QuinAPSO product are obtained, usually over a period of from several hours to several weeks. Typical effective crystallization times are from about 2 hours to 30 days with from about 4 hours to about 20 days being generally employed to obtain QuinAPSO products. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the QuinAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (M _w Al _χ P _y Si _z )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300; and "w", "x", "y", and "z" represent the mole fractions of elements M, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is

*-* selected such that the mole -fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Fraction Poini

F G H I J

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. QuinAPSO compositions were prepared using numerous regents; the appropriate sources of the various elements M are the same as those used in the preparation of the various APO and APSO molecular sieves containing the same elements, as described in detail above and below.

Reagents which may be employed to prepare QuinAPSOs include:

(a) Alipro: aluminum isopropoxide;

(b) LUDOX-LS: LUDOX-LS is the tradename of DuPont for an aqueous solution of 30

weight percent Si0 ₂ and 0.1 weight percent Na.O,**

(c) H..PO.: 85 weight percent phosphoric acid;

(d) MnAc: Manganese acetate, Mn(C ₂ H ₃ 0 ₂ ) ₂ .4H ₂ 0 (for QuinAPSOs containing manganese) ;

(e) CoAc: Cobalt Acetate, Co(C ₂ H ₃ 0 ₂ ) ₂ *-4H ₂ 0 (for QuinAPSOs containing cobalt) ;

(f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; and

(g) Pr ₂ NH: di-n-propylamine, (C_H ₇ ) ₂ NH.

Preparative Procedures QuinAPSOs may be prepared by forming a starting reaction mixture by adding H ₃ PO. and one half of the quantity of water. To this mixture an aluminum isopropoxide is added. This mixture is then blended until a homogeneous mixture is observed. To this mixture a silica (e.g., LUDOX-LS) is added and the resulting mixture blended (about 2 minutes) until a homogeneous mixture is observed. A second mixture is prepared using manganese acetate (or a appropriate source of another element M) and one half of the remaining water. A third mixture is prepared using cobalt acetate (or a appropriate source of another element M) and one half of the remaining water. The three mixtures are admixed and the resulting mixture

blended until a homogeneous mixture is observed. The organic templating agent is .then added to the resulting mixture and the resulting mixture blended until a homogeneous mixture is observed, i.e., about 2 to 4 minutes. The pH of the mixture is measured and adjusted for temperature. The mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at an effective temperature for an effective time. Digestions are typically carried out under autogenous pressure.

CoMnMσAPSO MOLECULAR SIEVES The CoMnMgAPSO senary molecular sieves of U.S. Serial No. 600,182, filed April 13, 1984, and of U.S.

Serial No. 57,648 filed June 9, 1987, have three-

_ dimensional microporous framework structures of Co0 ₂ ,

Mn0 ₂ —2, Mg0 ₂ —2, A10 ₂ , P0 ₂ and Si0 ₂ tetrahedral oxide units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Cc-*-Mn _u Mg _v Al _x PySi _z )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of (CotMn _u Mg _v Al _x P _y Si _z )0 ₂ and has a value of from zero (0) to about 0.3; "t", "u", and "v", "x", "y" and "z" represent the mole fractions of cobalt, manganese, magnesium, aluminum, phosphorus and silicon,

respectively, present as tetrahedral oxides and each has a value of at least 0.01. The mole fractions "t", "u", "v", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows (where w = t + u + v) :

Mole F Point A B C D E

In a preferred subclass of the CoMnMgAPSO molecular sieves the values of "w", "x", "y" and "z" in the above formula are within the limiting compositional values or points as follows:

Mole Fraction

Point x X (z + w) a 0.55 0.41 0.04 b 0.41 0.55 0.04 c 0.10 0.55 0.35 d 0.55 0.10 0.35

CoMnMgAPSO compositions are generally synthesized by hydrothermal.crystallization from a reaction mixture containing reactive sources of cobalt, manganese, magnesium, aluminum, phosphorus and silicon, and preferably an organic templating agent, i.e., structure-directing, agent. The structure-directing agents are preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between 50 ^β C and 250*C, and preferably between 100*C and 200*C, until crystals of the CoMnMgAPSO product are obtained, usually over a period of from several hours to several weeks. Typical crystallization times are from about 2 hours to about 30 days with from about 4 hours to about 20 days generally being employed to obtain CoMnMgAPSO products. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the CoMnMgAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: ^' aR : (Co _t Mn _u Mg _v Al _χ P _y Si ₂ )0 ₂ : bH.,0

wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6 and more preferably from greater than zero to about 2; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300; and "t", "u", "v", "x", "y", and "z" represent the mole fractions of cobalt, manganese, magnesium, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In a preferred embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z", where "w" is the sum of "t" + "u" + "v", are generally defined as being within the limiting compositional values or points as follows: e act Point F G H I J

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "t", "u", "v", "x", "y" and "z" such

that (t + u + v + x + y + z) = 1.00 mole. ^" Molecular sieves containing cobalt, manganese, ^" magnesium, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows: Preparative Reagents

CoMnMgAPSO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare CoMnAPSOs include:

(a) Alipro: aluminum isopropoxide; (b) LUDOX-LS: LUDOX-LS is the tradename of Du

Pont for an aqueous solution of 30 weight percent SiO_ and 0.1 weight percent Na_0; (c) H ₃ P0 ₄ : aqueous solution which is 85 weight percent phosphoric acid; (d) MnAc: Manganese acetate,

Mn(C ₂ H ₃ 0 ₂ ) ₂ .4H ₂ 0;

(e) CoAc: Cobalt Acetate, Co(C ₂ H ₃ 0 ₂ ) ₂ .4H ₂ 0;

(f) MgAc: Magnesium Acetate Mg(C ₂ H ₃ 0 ₂ ) .4H ₂ 0;

(g) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; and

(h). Pr ₂ NH: di-n-propylamine, (C ₃ H _? ) ₂ NH.

Preparative Procedures CoMnMgAPSOs -may be prepared by forming a starting reaction mixture by adding H ₃ P0 ₄ and one half of the quantity of water. To this mixture an aluminum isopropoxide is added. This mixture is then blended

until a homogeneous mixture is observed. To this mixture a silica (e.g., LUDOX-LS) is added and the resulting mixture blended (about 2 minutes) until a homogeneous mixture is observed. Three additional mixtures are prepared using cobalt acetate, magnesium acetate and manganese acetate using one third of the remainder of the water for each mixture. The four, mixtures are then admixed and the resulting mixture blended until a homogeneous mixture is observed. An organic templating agent is then added to the resulting mixture and the resulting mixture blended until a homogeneous mixture is observed, i.e., about 2 to 4 minutes. The mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature for a time.

Digestions are typically carried out under autogenous pressure.

SenAPSO MOLECULAR SIEVES The SenAPSO molecular sieves of U.S. Serial No. 600,183, filed April 13, 1984 have three-dimensional microporous framework structures of M0 ₂ , A10 ₂ ^"" , P0 ₂ and SiO, tetrahedral oxide units, where "n" is -3, -2, -1, 0 or +1, and have an empirical chemical composition on an anhydrous basis expressed by the formula: ^' mR : (M _w Al _χ P _y Si ₂ )0 ₂

wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; " " represents the molar amount of "R" present per mole of

(MwAIxPySiJ2 O •,___ _* , and has a value of from zero to about 0.3; "M" represents three elements selected from the group consisting of arsenic, beryllium, boron, chromium, cobalt, gallium, germanium, iron, lithium, magnesium, manganese, titanium, vanadium and zinc; "n" may have the aforementioned values depending upon the oxidation state of "M"; and "w", "x", "y" and "z" represent the mole fractions of elements "M", aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows, wherein "w" denotes the combined mole fractions of the three elements "M" such that "w" = "w** ¹ + "w ₂ " + "w ₃ " and each element "M" has a mole fraction of at least 0.01:

Mole Fraction Point A B C D E

In a preferred subclass of the SenAPSO molecular sieves the values of "w", "x", "y" and "z" in the above formula are within the limiting compositional values or points as follows:

Mole Fract o

SenAPSO compositions are generally synthesized by hydrothermal. crystallization from a reaction mixture containing reactive sources of elements "M", aluminum, phosphorus and silicon, and preferably an organic templating, i.e., structure-directing, agent. The structure-directing agents are preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between 50*C and 250°C, and preferably between 100'C and 200 ^β C, until crystals of the SenAPSO product are obtained, usually

over a period ^" of from several hours to several weeks. " Typical crystallization times are from about 2 hours to about 30 days with from about 4 hours to about 20 days generally being employed to obtain SenAPSO products. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the SenAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (M _w Al _χ P _y Si ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6 and more preferably from greater than zero to about 2; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300; and "w", "x", "y", and "z" represent the mole fractions of elements "M", aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01, with the proviso that each "M" is present in a mole fraction of at least 0.01. In a preferred embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" arid "z" are generally defined as being within the limiting compositional values or points as follows:

Point

F

G H

I

J

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w ^• + x ^• + y + z) = 1.00 mole. The SenAPSO molecular sieves are prepared by preparative techniques, and using sources of the elements "M" similar to those described for the other APSO molecular sieves described above and below. AsAPSO MOLECULAR SIEVES

The AsAPSO molecular sieves of U.S. Serial No.

599,808, filed April 13, 1984, and U.S. Serial No.

845,484 filed March 31, 1986 have a framework structure of As0 ₂ ^π , A10 ~, P0 ₂ and Si0 ₂ tetrahedral units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (As _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(AswAlxPySiz)02_ and has a value of zero to about 0.3,

but is preferably not greater than ^" 0.15; and "w", "x", "y" and "z" represent the mole fractions of the elements arsenic, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. The mole fractions "w", "x", "y" and "z"- are generally defined as being within the limiting compositional values or points as follows: e c o Point A B C D E

In a preferred subclass of the AsAPSO molecular sieves, the values of w, x, y and z are as follows:

Point a b c d e f

^' In an especially preferred ^" subclass of the AsAPSO molecular sieves, the values of w, x, y and z are as follows:

Mo

AsAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of arsenic, silicon, aluminum and phosphorus, preferably an organic templating, i.e. , -structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50*C and about 250*C, and preferably between about 100"C and about 200 ' C until crystals of the AsAPSO product are obtained, usually a period of from several hours to several weeks. Typical effective

-73- ti es of from 2 hours to about 30 days, generally from about 12 hours to about 10 days, have been observed. The product is- recovered by any convenient method such as centrifugation or filtration. In synthesizing the AsAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : _. (As _w Al _χ P _y Si ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 1.0; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 60; and "w", "x", "y" and "z" represent the mole fractions of arsenic, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01. In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values.or points as follows:

Point F G H

I J

Especially preferred reaction mixtures are those containing from about 1 to about 2 total moles of silicon and arsenic, and from about 1 to about 2 moles of aluminum, per mole of phosphorus.

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing arsenic, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents AsAPSO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare AsAPSOs include:

(a) Alipro: aluminum isopropoxide;

(b) CATAPAL: Trademark of Condea Corporation for hydrated pseudoboehmite;

(c) LUDOX-LS: LUDOX-LS is the tradehame of DuPont for an aqueous solution of 30 weight percent Si0 ₂ and 0.1 weight percent Na ₂ 0; (d) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid; (e). As ₂ 0 ₅ , arsenic(V) oxide;

(f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; (g) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (h) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH; (i) P ₃ N: tri-n-propylamine, (C ₃ H ₇ ) ₃ ; (j) Quin: Quinuclidine, (C.-H--N) ; (k) MQuin: Methyl Quinuclidine hydroxide,

(C _? H ₁₃ NCH ₃ OH) ; (1) C-hex: cyclohexylamine; (m) TMAOH: tetramethylammonium hydroxide; (n) TPAOH: tetrapropylammonium hydroxide; and (o) DEEA: 2-diethylaminoethanol;

(p) Tetraalkylorthosilicates, such as tetraethylorthosilicate. Preparative Procedures AsAPSOs may be prepared by forming a starting reaction mixture by dissolving the arsenic(V) oxide and the H ₃ P0 ₄ in at least part of the water. To this

solution the aluminum isopropoxide or CATAPAL is ^" added. This mixture is then blended until a homogeneous mixture is observed. To this mixture the templating agent and then the silica is added and the resulting mixture blended until a homogeneous mixture is observed. The mixture is then placed in a lined (polytetrafluoro¬ ethylene) stainless steel pressure vessel and digested at a temperature (150 ^* C or 200*C) for a time or placed in lined screw top bottles for digestion at 100*C. Digestions are typically carried out under autogenous pressure.

BAPSO MOLECULAR SIEVES

The BAPSO molecular sieves of U.S. Serial No. 600,177, filed April 13, 1984, and U.S. Serial No. 845,255 filed March 28, 1986 have a framework structure of BO ~, A10 ~, P0 ₂ and Si0 ₂ tetrahedral uriits having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (B _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(Bw.A1xPySiz„)02_ and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "w", "x", "y" and "z" represent the mole fractions of the elements boron, aluminum, phosphorus and silicon, respectively,

present as tetrahedral oxides. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mo e F c o Point A B C D E

In a preferred subclass of the BAPSO molecular- sieves, the values of w, x, y and z are as follows: e ct

Point a b c d e f

In an especially preferred subclass of the BAPSO molecular sieves, the values of w, x, y and z are as follows:

BAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of boron, silicon, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50"C and about 250"C, and preferably between about 100 ^β C and about 200 ^β C until crystals of the BAPSO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 20 days, have been observed. The product is recovered

by any convenient method such as centrifugation or ^" filtration.

In synthesizing the BAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows:

^{511 : (B} w ^A1 x ^P y ^Si z ⁾⁰ 2 ^{: bH} 2° wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.5;

"b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 20; and "w", "x", "y" and "z" represent the mole fractions of boron, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point F G H I J

Especially preferred reaction mixtures are those containing from about 1.0 to about 2 total moles of silicon and boron, and from about 0.75 to about 1.25 moles of aluminum, per mole of phosphorus.

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing boron, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents BAPSO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare BAPSOs include:

(a) Alipro: aluminum isopropoxide;

(b) CATAPAL: Trademark of Condea Corporation for hydrated pseudoboehmite;

-3.6- (c) LUDOX-LS: LUDOX-LS is the tradename of ^" DuPont for an aqueous solution of 30 weight percent SiO_ and 0.1 weight percent Na ₂ C (d) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid; (e). H ₃ B0 ₃ , boric acid, and trialkyl borates; (f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; (g) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (h) Pr ₂ NH: di-n-propylamine, (C ₃ H _? ) ₂ NH; (i) Pr ₃ N: tri-n-propylamine, (C.,H ₇ ) ₃ N; (j) Quin: Quinuclidine, (α_H ₁₃ N) ; (k) MQuin: Methyl Quinuclidine hydroxide,

(C _? H ₁₃ NCH ₃ OH) ; (1) C-hex: cyclohexylamine; (m) TMAOH: tetramethylammonium hydroxide; (n) TPAOH: tetrapropylammonium hydroxide; and (o) DEEA: 2-diethylaminoethanol;

(p) Tetraalkylorthosilicates, such as tetraethylorthosilicate. Preparative Procedures BAPSOs may be prepared by forming a starting reaction mixture by dissolving aluminum isopropoxide in an alcohol such as isopropanol, adding the H ₃ P0 ₄ and

recovering the solid which precipitates. This solid is then added to water, and trialkylborate (for example trimethyl borate added, followed by silica and the templating agent. This mixture is then blended until a homogeneous mixture is observed. The mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150 ^β C or 200"C) for a time or placed in lined screw top bottles for digestion at 100*C. Digestions are typically carried out under autogenous pressure.

BeAPSO MOLECULAR SIEVES The BeAPSO molecular sieves of U.S. Serial No. 600,176, filed April 13, 1984, and U.S. Serial No.

841,752 filed March 20, 1986 have a framework structure of Be0 ₂ —2, A10 ₂ —, P0 ₂ + and Sι0 ₂ tetrahedral units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Be _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of O. -ώ and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "w", "x", "y" and "z" represent the mole fractions of the elements beryllium, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. The mole

.-38- fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point A B C D E

In a preferred subclass of the BeAPSO molecular sieves, the values of w, x, y and z are as follows:

Point a b c d e f

BeAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of beryllium, silicon, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably

-39- a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50'C and about 250*C, and preferably between about 100*C and about 200*C, until crystals of the BeAPSO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours. to about 30 days, generally from about 4 hours to about 20 days, have been observed, with from 1 to 10 days being preferred. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the BeAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Be _w Al _χ P _y Si ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.5; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most

preferably not greater than about 20; and "w", "x", "y" and "z" represent the mole fractions of beryllium, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Fraction

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x ^ι: , "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing beryllium, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents BeAPSO _. compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare BeAPSOs include:

(a) Alipro: aluminum isopropoxide;

(b) CATAPAL: Trademark of Condea Corporation for hydrated pseudoboehmite;

(c) LUDOX-LS: LUDOX-LS is the tradename of DuPont for an aqueous solution of 30 weight percent Si0 ₂ and 0.1 weight percent Na ₂ 0;

(d) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid;

(e beryllium sulfate, BeS0 ₄ ; (f TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(g TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(h Pr ₂ NH: di-n-propylamine, (C ₃ H _? ) ₂ NH; (i Pr ₃ N: tri-n-propylamine, (C ₃ H ₇ ) ₃ N; (j Quin: Quinuclidine, (C..H--N) ;

MQuin: Methyl Quinuclidine hydroxide,

(C _? H ₁₃ NCH ₃ OH) ;

(1 C-hex: cyclohexylamine; (m TMAOH: tetramethylammonium hydroxide; (n TPAOH: tetrapropylammonium hydroxide; and (o DEEA: 2-diethylaminoethanol; (P Tetraalkylorthosilicates, such as tetraethy1orthosilicate.

Preparative Procedures BeAPSOs may be prepared by forming a starting solution by mixing H ₃ P0 ₄ in at least part of the water. To this solution is added beryllium sulfate (or another beryllium salt) and the resultant mixture stirred until a homogeneous solution is obtained. To this solution may be added successively the aluminum oxide,- the silica and the templating-agent, with the mixture being stirred between each addition until it is homogeneous. The mixture is then placed in a lined (polytetrafluoro¬ ethylene) stainless steel pressure vessel and digested at a temperature (150 ^* C or 200*C) for a time or placed in lined screw top bottles for digestion at 100 ^β C. Digestions are typically carried out under autogenous pressure.

CAPSO MOLECULAR SIEVES The CAPSO molecular sieves of U.S. Serial No. 599,830, filed April 13, 1984, and U.S. Serial No. 852,174 filed April 15, 1986 have a framework structure of Cr0 ₂ ⁿ , A10 ~, P ₂ ⁺ and Si0 ₂ tetrahedral units (where "n" is -1, 0 or +1) having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Cr _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intraerystalline pore system; "m"

represents the molar amount of "R" present per mole of

(Crw,A1xPySiz O2. and has a va,lue of zero to about 0.3,' but is preferably not greater than 0.15; and "w", "x", "y" and "z" represent the mole fractions of the elements chromium, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows: Mole F actio

Point A B C D E

In a preferred subclass of the CAPSO molecular sieves, the values of w, x, y and z are as follows:

M e F action Point a b c d e f

In an especially preferred subclass of the CAPSO molecular sieves, the values of x and y in the above formula are each within the range of about 0.4 to 0.5 and (z + w) is in the range of about 0.02 to 0.15. Since the exact nature of the CAPSO molecular sieves is not clearly understood at present, although all are believed to contain Cr0 ₂ tetrahedra in the three-dimensional microporous crystal framework structure, it is advantageous to characterize the CAPSO molecular sieves by means of their chemical composition. This is due to the low level of chromium present in certain of the CAPSO molecular sieves prepared to date which makes it difficult to ascertain the exact nature of the interaction between chromium, aluminum, phosphorus and silicon. As a result, although it is believed that Cr0 ₂ tetrahedra are substituted isomorphously for A10 ₂ , P0 ₂ or Si0 ₂ tetrahedra, it is appropriate to characterize certain CAPSO compositions by reference to their chemical composition in terms of the mole ratios of oxides.

CAPSO compositions are generally synthesized by .hydrothermal crystallization from a reaction mixture containing reactive sources of chromium, silicon, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic

Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50 ^β C and about 250*C, and preferably between abou 100*C and about 200"C, until crystals of the CAPSO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 20 days, and preferably about 1 to about 10 days, have been observed. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the CAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Cr _w Al _χ P _y Si _z )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.5; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 20; and "w", "x", "y"

and "z" represent the mole fractions of chromium, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional' values or points as follows: a Point F G H I J Especially preferred reaction mixtures are those containing from about 0.3 to about 0.5 total moles of silicon and chromium, and from about 0.75 to about 1.25 moles of aluminum, .per mole of phosphorus.

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing chromium, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents CAPSO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare MnAPSOs include: (a) Alipro: aluminum isopropoxide;

(b) CATAPAL: Trademark of Condea Corporation for hydrated pseudoboehmite;

(c) LUDOX-LS: LUDOX-LS is the tradename of DuPont for an aqueous solution of 30 weight percent Si0 ₂ and 0.1 weight percent Na ₂ 0;

(d) H.P0 ₄ : 85 weight percent aqueous phosphoric acid;

(e) chromium acetate, and chromium acetate hydroxide;

(f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(g) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (h) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH;

(i) Pr ₃ N: tri-n-propylamine, (C ₃ H ₇ ) ₃ N;

(j) Quin: Quinuclidine, (C..H--N) ;

(k) MQuin: Methyl Quinuclidine hydroxide, (C _? H ₁₃ NCH ₃ OH) ; (1) C-hex: cyclohexylamine;

(m) TMAOH: tetramethylammonium hydroxide;

(n) TPAOH: tetrapropylammonium hydroxide; and (o) DE-EA: 2-diethylaminoethanol; (p) Tetraalkylorthosilicates, such as tetraethylorthosilicate. Preparative Procedures

CAPSOs may be prepared by forming a starting solution by dissolving H ₃ P0 ₄ in at least part of the water. To this solution the aluminum isopropoxide is added. This mixture is then blended until a homogeneous mixture is observed. To this mixture the silica, the chromium acetate or chromium acetate hydroxide and the templating agent are successively added and at each step the resulting mixture is blended until a homogeneous mixture is observed. Alternatively, the water and aluminum isopropoxide may first be mixed, and then the silica, the chromium acetate or chromium acetate hydroxide, the phosphoric acid and the templating agent added, and again at each step the resulting mixture is blended until a homogeneous mixture is observed.

In either case, the mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150"C or 200*C) for a time or placed in lined screw top bottles for digestion at 100*C. Digestions are typically carried out under autogenous pressure.

GaAPSO MOLECULAR SIEVES

The GaAPSO molecular sieves of U.S. Serial No.

599,925, filed April 13, 1984, and U.S. Serial No.

845,985 filed March 31, 1986 have a framework structure of GaO ~, A10 ~, PO and SiO tetrahedral units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Ga _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intraerystalline pore system; "m" represents the molar amount of "R" present per mole of

(GawAlxPySiz)02_ and has a value of zero to about 0.3, but is preferably not greater than 0.2; and "w", "x", "y" and "z" represent the mole fractions of the elements gallium, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Fraction Point x Y ( z + w)

A 0.60 0.38 0.02

B 0.38 0.60 0.02

C 0.01 0.60 0.39

D 0.01 0.01 0.98 E 0.60 0.01 0.39

In a preferred subclass of the GaAPSO molecular sieves, the values of w, x, y and z are as follows:

Point a b c d e f

In an especially preferred subclass of the GaAPSO molecular sieves, the values of w, x, y and z are as follows:

Point g h i j k

1

GaAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of gallium, silicon, aluminum and phosphorus, preferably an organic

templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably urider autogenous pressure at a temperature between about 50*C- and about 250 ^β C, and preferably between about 100 ^* C and about 200 ^* C, until crystals of the GaAPSO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 20 days, and preferably about 2 to about 15 days, have been observed. The product is recovered by any convenient method such as centrifugation or ^' filtration.

In synthesizing the GaAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows:

aR : ^(Ga _w ^A1 x ^P y ^Si z ⁾⁰ 2 ^{: bH} ₂ ° wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 1.0;

"b" has a value of from zero (0) to about 500,

preferably between about 2 and about 300, most preferably not greater than -about 20; and "w", "x", "y" ^" and "z" represent the mole fractions of gallium, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows: Mole Fraction

Point F G H I J

Especially preferred reaction mixtures are those containing from about 0.5 to about 1.0 total moles of silicon and gallium, and from about 0.75 about 1.25 moles of aluminum, per mole of phosphorus.

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing gallium, aluminum, phosphorus and silicon as

fra ework tetrahedral oxide units are prepared as follows:

Preparative Reagents GaAPSO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare GaAPSOs include:

(a) ^• Alipro: aluminum isopropoxide; (b) CATAPAL: Trademark of Condea Corporation for hydrated pseudoboehmite; (c) LUDOX-LS: LUDOX-LS is the tradename of

DuPont for an aqueous solution of 30 weight percent Si0 ₂ and 0.1 weight percent N ₂ 0;

(d) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid;

(e) gallium hydroxide, or gallium sulfate;

(f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(g) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(h) Pr ₂ NH: di-n-propylamine, (C ₃ H _? ) ₂ NH;

(i) r ₃ N: tri-n-propylamine, (C ₃ H ₇ ) ₃ N;

(j) Quin: Quinuclidine, (C-H..N) ;

(k) MQuin: Methyl Quinuclidine hydroxide, (C _? H ₁₃ NCH ₃ OH), '

(1) C-hex: cyclohexylamine;

(m) TMAOH: tetramethylammonium hydroxide; (n) TPAOH: tetrapropylammonium hydroxide; and (o) DEEA: 2-diethylaminoethanol; (p) Tetraalkylorthosilicates, such as tetraethylorthosilicate.

Preparative Procedures GaAPSOs may be prepared by forming a starting solution by dissolving the H ₃ PO in at least part of the water. To this solution the aluminum hydroxide or isopropoxide is added. This mixture is then blended until a homogeneous mixture is observed. To this mixture is added a second solution prepared by adding silica to a solution containing the gallium hydroxide and the templating agent and then the combined mixture is blended until a homogeneous mixture is observed.

Alternatively, the templating agent may be added to the solution containing the phosphoric acid and water, and a solution of gallium sulfate in water added, followed by successive additions of silica and aluminum oxide and then the combined mixture is blended until a homogeneous mixture is observed.

In either case, the mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150°C or 200*C) for a time or placed in lined screw top bottles

for digestion at 100'C. Digestions are typically carried out under autogenous pressure.

GeAPSO MOLECULAR SIEVES

The GeAPSO molecular sieves of U.S. Serial No. 599,971, filed April 13, 1984, and U.S. Serial No.

852,175 filed April 15, 1986 have a framework structure of Ge0 ₂ , A10 ~, P0 ₂ and Si0 ₂ tetrahedral units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Ge _w Al _χ P _y Si _z )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(GewAl J_PySi ww)0 Λ» ^' and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "w", "x",

"y" and "z" represent the mole fractions of the elements germanium, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point A B C

D E

In a preferred subclass of the GeAPSO molecular sieves, the values of w, x, y and z are as follows:

Point a b c d e f

In an especially preferred subclass of the GeAPSO molecular sieves, the values of w, x, y and z are as follows:

GeAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of germanium, silicon, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50 ^β C and about 250 ^β C, and preferably between about 100 " C and about 200*c until crystals of the GeAPSO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 20 days, and preferably about 12 hours to about 7 days have been observed. The product

is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the GeAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Ge _w Al _χ P _y Si ₂ )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.5; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 20, and desirably not greater than about 10; and "w", ^» x", "y" and "z" represent the mole fractions of germanium, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Especially preferred reaction mixtures are those containing from about 0.2 to about 0.3 total moles of silicon and germanium, and from about 0.75 to about 1.25 moles of aluminum, per mole of phosphorus.

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing germanium, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents GeAPSO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare GeAPSOs include:

(a) Alipro: aluminum isopropoxide;

(b) CATAPAL: Trademark of Condea Corporation for hydrated pseudoboehmite;

(c) LUDOX-LS: LUDOX-LS is the tradename of DuPont for an aqueous solution of 30 weight percent Si0 ₂ and 0.1 weight percent Na ₂ 0; (d) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid;

(e) ^' germanium tetrachloride or germanium ethoxide;

(f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(g) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(h) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH;

(i) Pr ₃ N: tri-n-propylamine, (C ₃ H _? ) ₃ N; (j) Quin: Quinuclidine, (C ₇ H. ₃ N) ;

(k) MQuin: Methyl Quinuclidine hydroxide, (C ₇ H ₁₃ NCH ₃ OH) ;

(1) C-hex: cyclohexylamine;

(m) TMAOH: tetramethylammonium hydroxide; (n) TPAOH: tetrapropylammonium hydroxide; and

(o) DEEA: 2-diethylaminoethanol;

(p) Tetraalkylorthosilicates, such as tetraethylorthosilicate;

(q) aluminum chlorhydrol.

Preparative Procedures In some cases, it may be advantageous, when synthesizing the GeAPSO compositions, to first combine sources of germanium and aluminum, or of germanium, aluminum and silicon, to form a mixed germanium/aluminum or germanium/aluminum/silicon compound (this compound being typically a mixed oxide) and thereafter to combine this mixed compound with a source of phosphorus to form the final GeAPSO composition. Such mixed oxides may be prepared for example by hydrolyzing aqueous solutions containing germanium tetrachloride and aluminum chlorhydrol, or germanium ethoxide, tetraethylorthosilicate, and aluminum tri-sec-butoxide. GeAPSOs may be prepared by forming a starting solution by dissolving the H ₃ P0 ₄ in at least* part of the water. To this solution the aluminum isopropoxide or CATAPAL is added. This mixture is then blended until a homogeneous mixture is observed. To this mixture the templating agent and then a solution containing tetraethylorthosilicate and germanium ethoxide, and the resulting mixture blended until a homogeneous mixture is observed.

Alternatively, the phosphoric acid may first be mixed with the templating agent, and then a solution containing tetraethylorthosilicate and germanium ethoxide combined with the phosphoric acid/templating

agent solution. Then the aluminum oxide is added and the resultant mixture blended until homogeneous.

In a third procedure, the phosphoric acid may first be mixed with the templating agent and water, and to the resultant solution is added the solid aluminum/ silicon/germanium mixed oxide prepared as described above. The resultant mixture is then blended until homogeneous.

Whichever procedure is adopted, the final mixture is then placed in a lined (polytetrafluoro¬ ethylene) stainless steel pressure vessel and digested at a temperature (150 ^β C or 200*C) for a time or placed in lined screw top bottles for digestion at 100'C. Digestions are typically carried out under autogenous pressure.

LiAPSO MOLECULAR SIEVES The LiAPSO molecular sieves of U.S. Serial No. 599,952, filed April 13, 1984, and U.S. Serial No.

847,227 filed April 2, 1986 have a framework structure of Li0 ₂ —3, A10 ₂ —, P0 ₂ + and Si0 ₂ tetrahedral units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Li _w Al _χ P _y Si ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(LiwAlxPySiz)02- and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "w", "x", "y" and "z" represent the mole fractions of the elements lithium, aluminum, phosphorus and silicon, respectively, present as tetrahedral oxides. The mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows: e ract o Point A

B

C

D

E In a preferred subclass of the LiAPSO molecular sieves, the values of w, x, y and z are as follows:

Point a b c d e f

In an especially preferred subclass of the LiAPSO molecular sieves, the ^' value of w+z is not greater than about 0.20.

Since the exact nature of the LiAPSO molecular sieves is not clearly understood at present, although all are believed to contain LiO_ tetrahedra in the three-dimensional microporous crystal framework structure, it is advantageous to characterize the LiAPSO molecular sieves by means of their chemical composition. This is due to the low level of lithium present in certain of the LiAPO molecular sieves prepared to date which makes it difficult to ascertain the exact nature of the interaction between lithium, aluminum, phosphorus and silicon. As a result, although it is believed that 'i-- _'2 tetrahedra are substituted isomorphously for A10 ₂ , P0 ₂ or Si0 ₂ tetrahedra, it is appropriate to characterize certain LiAPSO compositions by reference to their chemical composition in terms of the mole ratios of oxides. LiAPSO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of lithium, silicon, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent', preferably a compound of an element of Group VA of the Periodic

Table, and/or optionally an alkali or other metal. The

reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50"C and about 250 ^* C, and preferably between about 100"C and about 200"C until crystals of the LiAPSO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 20 days, and preferably about 1 to about 10 days, have been observed. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the LiAPSO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Li _w Al _χ P _y Si ₂ )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.5; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 20, and most desirably not greater than about 10; and "w", "x", "y" and "z"

represent the mole fractions of lithium, aluminum, phosphorus and silicon, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "w", "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole act on Point F G H I J In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "w", "x", "y" and "z" such that (w + x + y + z) = 1.00 mole. Molecular sieves containing lithium, aluminum, phosphorus and silicon as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents LiAPSO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare Li-APSOs include:

(a) Alipro: aluminum isopropoxide;

(b) CATAPAL: Trademark of Condea Corporation for hydrated pseudoboehmite;

(c) LUDOX-LS: LUDOX-LS is the tradename of DuPont for an aqueous solution of 30 weight percent Si0 ₂ and 0.1 weight percent Na ₂ 0;

(d) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid;

(e) lithium orthophosphate; (f) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; (g) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (h) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH; (i) Pr ₃ N: tri-n-propylamine, (C.,H ₇ ) ₃ N;

(j) Quin: Quinuclidine, (C ₇ H__N) ; (k) MQuin: Methyl Quinuclidine hydroxide,

(C _? H ₁₃ NCH ₃ OH) ; (1) C-hex: cyclohexylamine; (m) TMAOH: tetramethylammonium hydroxide;

(n) TPAOH: tetrapropylammonium hydroxide; and (o) DEEA: 2-diethylaminoethanol; (p) Tetraalkylorthosilicates, such as tetraethylorthosilicate. Preparative Procedures

LiAPSOs may be prepared by forming a starting

-US- reaction mixture mixing lithium phosphate and aluminum oxide, then adding the resultant mixture to the H ₃ P0 ₄ . To the resultant mixture is added silica and the templating agent and the resulting mixture is blended until a homogeneous mixture is observed. The mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150*C or 200*C) for a time or placed in lined screw top bottles for digestion at 100*C. Digestions are typically carried out under autogenous pressure.

A1PO._ ALUMINOPHOSPHATE MOLECULAR SIEVES

The A1P0 ₄ aluminophosphate molecular sieves of U.S. Patent No. 4,310,440 and U.S. Serial No. 880,559, filed June 30, 1986 are disclosed as microporous crystalline aluminophosphates having an essential crystalline framework structure whose chemical composition, expressed in terms of molar ratios of oxides, is: ^A1 ₂ ° ₃ ^{: O} - ⁸ " ¹ - ^{2 p} 2°5'

The pores of the framework structure are uniform and in each species have nominal diameters of from 3 to 10

Angstroms; the aluminophosphates have an intracrystalline adsorption capacity for water at 4.6 Torr and 24*C of at least 3.5 weight percent, the adsorption of water being completely reversible while

retaining the same essential framework topology in both the hydrated and dehydrated -state. By the term "essential framework topology" is meant the spatial arrangement of the primary Al-0 and P-0 bond linkages. No change in the framework topology indicates that there is no disruption of these primary bond linkages. The' luminophosphates are prepared by hydrothermal crystallization of a reaction mixture prepared by combining a reactive source of phosphate, alumina and water and at least one structure-directing or templating agent which can include an organic amine and a quaternary ammonium salt. In the as-synthesized form, the structure-directing agent is contained within the framework structure of the aluminophosphate in amounts which vary from species to species hut usually do not exceed one mole per mole of 1 ₂ 0 ₃ thereof. This structure-directing agent is readily removed by water washing or calcination and does not appear to be an essential constituent of the aluminophosphate, as evidenced by essentially complete absence of ion- exchangeability of the as-synthesized compositions and also the complete absence of any internally-contained organic molecules in the. as-synthesized form of at least one species of the generic class. Evidence that structure-directing agent is a critical constituent is contained in certain of the Examples of the Patent

4,310,440, wherein reaction mixtures, otherwise identical to those which yield the A1P0 ₄ products except for the presence of templating agents, yield instead the previously known aluminophosphate phases A1PO..1.1-1.3 ^H ₂ °/ AlPO -tridymite, A1P0 ₄ -quartz and

A1PO4.-cristobalite.

The A1P0 ₄ aluminophosphates are prepared by forming a reaction mixture which contains, in terms of molar ratios of oxides: Al Δ.O-J : 0.5-1.5 P Δ.O..> : 7-100 H2_0 and contains from about 0.2 to 2.0 moles of templating agent per mole of A1 ₂ 0 ₃ . The reaction mixture is placed in a reaction vessel inert toward the reaction system and heated at a temperature of at least about 100 ^β C, preferably between 100*C and 300 ^* C, until crystallized, usually a period from 2 hours to 2 weeks. The solid crystalline reaction product is then recovered by any convenient method, such as filtration or centrifugation, washed with water and dried at a temperature between ambient and 110'C, preferably in air.

MeAPO MOLECULAR SIEVES MeAPO molecular sieves are crystalline microporous aluminophosphates in which the substituent metal is one of a mixture of two or more divalent metals of the group magnesium, manganese, zinc and cobalt and are disclosed in U.S. Patent No. 4,567,029. Members of

this novel class of compositions have a three- dimensional microporous crystal framework structure of

M0 ₂ —2, A10— ₂ and PO+ ₂ tetrahedral units and have an essential empirical chemical composition, on an anhydrous basis, of:

* ^{: (M} x ^A1 y ^P z ⁾⁰ 2 wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the moles of "R" present per mole of

(MxAl.yJPJz O-2 and has a value of from zero to 0.3, the maximum value in each case depending upon the molecular dimensions of the templating agent and the available void volume of the pore system of the particular metal aluminophosphate involved; "x", "y", and "z" represent the mole fractions of the metal "M", (i.e., magnesium, manganese, zinc and cobalt) , aluminum and phosphorus, respectively, present as tetrahedral oxides, said mole fractions being such that they are representing the following values for "x", "y", and "z": ction

When synthesized the minimum value of " " in the formula above is 0.02. In a preferred subclass of the metal aluminophosphates of this invention, the values of "x", "y" and "z" in the formula above are representing the following values for "x", "y" and "z":

Mole Fraction

Point x y_ z. a 0.01 0.52 0.47 b 0.01 0.39 0.60 c 0.25 0.15 0.60 d 0.25 0.40 0.35

The as-synthesized compositions are capable of withstanding 350"C calcination in air for extended periods, i.e., at least 2 hours, without becoming amorphous. While it is believed that the M, Al and P framework constituents are present in tetrahedral coordination with oxygen, it is theoretically possible that some minor fraction of these framework constituents are present in coordination with five or six oxygen atoms. It is not, moreover, necessarily the case that all of the M, Al and/or P content of any given synthesized product is a part of the framework in the aforesaid types of coordination with oxygen. Some of each constituent may be merely occluded or in some as yet undetermined form and may or may not be structurally significant.

Since the term "metal aluminophosphate" is somewhat cumbersome, particularly in view of the need for numerous repetitions thereof in describing such compositions, the "short-hand" reference "MeAPO" is employed hereinafter. Also in those cases where the metal "Me" in the composition is magnesium, the acronym MAPO is applied to the composition. Similarly, ZAPO, MnAPO, and CoAPO are applied to the compositions which contain zinc, manganese and cobalt, respectively. To identify the various structural species which make up each of the subgeneric classes MAPO, ZAPO, CoAPO and MnAPO, each species is assigned a number and is identified, for example, as ZAPO-5, MAPO-11, CoAPO-11 and so forth. The term "essential empirical chemical composition" is meant to include the crystal framework and can include any organic templating agent present in the pore system, but does not include alkali metal or other ions which can be present by virtue of being contained in the reaction mixture or as a result of post-synthesis ion-exchange. Such ionic species, when present, function primarily as charge-balancing ions for

A10- — and/or MO.—2 tetrahedra not associated with P0 ₂ +

tetrahedra or an organic ion derived from the organic templating agent.

The metal aluminophosphates ("MeAPOs") are synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of the metal "M", alumina and phosphate, an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and optionally an alkali metal. The reaction mixture is placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetra- fluorpethylene and heated, preferably under autogenous pressure at a temperature between 100*C and 225'C, and preferably between 100*C and 200 ' C, until crystals of the metal aluminophosphate product are obtained, usually a period of from 4 hours to 2 weeks. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the MeAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of molar ratios as follows: aR : (M _χ Al _y P ₂ )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" has a value great enough to constitute an effective concentration of "R" and is within the range of >0 to 6; "b" has a value of from zero to 500, preferably 2 to 30; "M" represents a metal of the group zinc, magnesium, manganese and cobalt, "x", "y" and "z" represent the

mole fractions, respectively, of "M", aluminum and phosphorus in the ( ^M _X ^A ***** _{V 2} )° ₂ constituent, and each has a value of at least 0.01, the said points E, F, G, H, I, and J representing the following values for "x", "y" and "z":

Point JC

E 0.01

F 0.01 G 0.29

H 0.40

I 0.40

J 0.29

In the foregoing expression of the reaction composition, the reactants are normalized with respect to a total of (M + Al + P) = (x + y + z) = 1.00 mole.

In forming the reaction mixture from which the metal aluminophosphates are crystallized the organic templating agent can be any of those heretofore proposed for use in the synthesis of conventional zeolite aluminosilicates and microporous aluminophosphates. In general these compounds contain elements of Group VA of the Periodic Table of Elements, particularly nitrogen, phosphorus, arsenic and antimony, preferably N or P and most preferably N, which compounds also contain at least one alkyl or aryl group having from 1 to 8 carbon atoms.

Particularly preferred nitrogen-containing compounds for use as templating agents are the amines and quaternary ammonium compounds, the latter being represented generally by the formula R ₄ N wherein each R is an alkyl or aryl group containing from 1 to 8 carbon atoms. Polymeric quaternary ammonium salts such as [(C ₁₄ H ₃₂ N ₂ ) (OH) ₂ ] wherein "x" has a value of at least 2 are also suitably employed. Both mono-, di- and triamines are advantageously utilized, either alone or in combination with a quaternary ammonium compound or other templating compound. Mixtures of two or more templating agents can either produce mixtures of the desired metal aluminophosphates or the more strongly directing templating species may control the course of the reaction with the other templating species serving primarily to establish the pH conditions of the reaction gel. Representative templating agents include tetra ethylammonium, tetraethy1ammonium, tetrapropylammonium or tetrabutylammonium ions; di-n-propylamine; tripropylamine; triethylamine; triethanolamine; piperidine; cyclohexyl mine; 2-methylpyridine; ,N-dimethylbenzylamine; N-N-dimethylethanolamine; choline; N,N'-dimethylpiperazine; 1,4-diazabicyclo (2,2,2) octane; N-methyldiethanolamine; N-methylethanolamine; N-methylpiperidine; 3- ethylpiperidine;

N-methylcyclohexylamine; 3-methylpyridine; 4-methylpyridine; quinuclidine;

N,N'-dimethyl-l,4-diazabicyclo (2,2,2) octane ion; di-n-butylamine, neopentylamine; di-n-pentylamine; isopropylamine; t-butylamine; ethylenediamine; pyrrolidine; and 2-imidazolidone. Not every templating agent will direct the formation of every species of metal aluminophosphate (MeAPO), i.e., a single templating agent can, with proper manipulation of the reaction conditions, direct the formation of several

MeAPO compositions, and a given MeAPO composition can be produced using several, different templating agents.

The preferred phosphorus source is phosphoric acid, but organic phosphates such as triethylphosphate have been found satisfactory, and so also have crystalline or amorphous aluminophosphates such as the A1P0 ₄ composition of U.S. Patent No. 4,310,440. Organo-phosphorus compounds, such as tetrabutyl- phosphonium bromide do not, apparently serve as reactive sources of phosphorus, but these compounds do function as templating agents. Conventional phosphorus salts such as sodium metaphosphate, may be used, at least in part, as the phosphorus source, but are not preferred. The aluminum source is preferably either an aluminum alkoxide, such as aluminum isopropoxide, or pseudoboehmite. The crystalline or amorphous

aluminophosphates which are a suitable source of phosphorus are, of course, also suitable sources of aluminum. Other sources of aluminum used in zeolite synthesis, such as gibbsite, sodium aluminate and aluminum trichloride, can be employed but are not preferred.

The- metals zinc, cobalt, magnesium and manganese can be introduced into the reaction system in any form which permits the formation in situ of reactive divalent ions of the respective metals. Advantageously salts, oxides or hydroxides of the metals are employed such as cobalt chloride hexahydrate, alpha cobaltous iodide, cobaltous sulfate, cobalt acetate, cobaltous bromide, cobaltous chloride, zinc acetate, zinc bromide, zinc formate, zinc iodide, zinc sulfate heptahydrate, magnesium acetate, magnesium bromide, magnesium chloride, magnesium iodide, magnesium nitrate, magnesium sulfate, manganous acetate, manganous bromide, manganous sulfate, and the like. While not essential to the synthesis of MeAPO compositions, it has been found that in general, stirring or other moderate agitation of the reaction mixture and/or seeding the reaction mixture with seed crystals of either the MeAPO species to be produced or a topologically similar aluminophosphate or

aluminosilicate composition, facilitates the crystallization procedure.

After crystallization the MeAPO product is isolated and advantageously washed with water and dried in air. The as-synthesized MeAPO contains within its internal pore system at least one form of the templating agent employed in its formation. Most commonly the organic moiety is present, at least in part, as a charge-balancing cation as is generally the case with as-synthesized aluminosilicate zeolites prepared from organic-containing reaction systems. It is possible, however, that some or all of the organic moiety is an occluded molecular species in a particular MeAPO species. As a general rule, the templating agent, and hence the occluded organic species, is too large to move freely through the pore system of the MeAPO product and must be removed by calcining the MeAPO at temperatures of 200"C to 700"C to thermally degrade the organic species. In a few instances the pores of the MeAPO product are sufficiently large to permit transport of the templating agent, particularly if the latter is a small molecule, and accordingly complete or partial removal thereof can be accomplished by conventional desorption procedures such as carried out in the case of zeolites. It will be understood that the term

¹¹ as-synthesized" as used herein does not include the

conditiσn of the MeAPO phase wherein the organic moiety occupying the intracrystalline pore system as a result of the hydrothermal crystallization process has been reduced by post-synthesis treatment such that the value of "m" in the composition formula: mR : (M _χ Al _y P ₂ )0 ₂ has a value of less than 0.02. The other symbols of the formula are as defined hereinabove. In those preparations in which an aluminum alkoxide is employed as the source of aluminum, the corresponding alcohol is necessarily present in the reaction mixture since it is a hydrolysis product of the alkoxide. It has not been determined whether this alcohol participates in the synthesis process as a templating agent. For the purposes of this application, however, this .alcohol is arbitrarily omitted from the class of templating agents, even if it is present in the as-synthesized MeAPO material.

Since the MeAPO compositions are formed from ^A10 • ^P0 ₂ *' ^ani -~ ^M0 ₂ tetreihedral units which, respectively, have a net charge of -1, +1, and -2, .the matter of cation exchangeability is considerably more complicated ^' than in the case of zeolitic molecular sieves in which, ideally, there is a stoichiometric relationship between A10 ₂ tetrahedra and charge-balancing cations. In the MeAPO compositions, an

A10 ₂ ~ tetrahedron can be balanced electrically either by association with a P0. ₂ tetrahedron or a simple cation such as an alkali metal cation, a cation of the metal "M" present in the reaction mixture, or an organic cation derived from the templating agent. Similarly an

M0 ₂ -2 tetrahedron can be balanced electrically by association with P0 ₂ tetrahedra, a cation of the metal "M", organic cations derived from the templating agent, or other divalent or polyvalent metal cations introduced from an extraneous source. It has also been postulated that non-adjacent A10 ~ and PO_ tetrahedral pairs can be balanced by Na and OH , respectively [Flanigen and Grose, Molecular Sieve Zeolites-I, ACS, Washington, D.C. (1971)]. FAPO MOLECULAR SIEVES

Ferroaluminophosphates are disclosed in U.S. Patent No. 4,554,143, incorporated herein by reference, and have a three-dimensional microporous crystal framework structure of Fe0 ₂ ⁿ , A10 ~ and P0 ₂ ⁺ tetrahedral units and have an essential empirical chemical composition, on an anhydrous basis, of: mR : (Fe _χ Al _y P ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; " " represents the moles of "R" present per mole of

(FexAlyPz)02« and has a value of from zero to 0.3, the

maxi um value in each case depending upon the molecular dimensions of the templating agent and the available void volume of the pore system of the particular ferroaluminophosphate involved; "x", "y", and "z" represent the mole fractions of iron, aluminum and phosphorus, respectively, present as tetrahedral oxides, representing the following values for "x", "y", and "z":

Mole Fraction Point A B C D When synthesized the minimum value of "m" in the formula above is 0.02. In a preferred subclass of the ferroaluminophosphates the values of "x", "y" and "z" in the formula above are representing the following values for "x", "y" and "z":

Point a b c d The iron of the Fe0 ₂ structural units can be in either the ferric or ferrous valence state, depending

largely upon the source of the iron in the synthesis gel. Thus, an FeO. tetrahedron in the structure can have a net charge of either -1 or -2. While it is believed that the Fe, Al and P framework constituents are present in tetrahedral coordination with oxygen (and are referred to herein as such) , it is theoretically possible that* some minor fraction of these framework constituents are present in coordination with five or six oxygen atoms. It is not, moreover, necessarily the case that all of the Fe, Al and/or P content of any given synthesized product is a part of the framework in the aforesaid types of coordination with oxygen. Some of each constituent may be merely occluded or in some as yet undetermined form, and may or may not be structurally significant.

For convenience in describing the ferroaluminophosphates, the "short-hand" acronym "FAPO" is sometimes employed hereinafter. To identify the various structural species which make up the generic class FAPO, each species is assigned a number and is identified, for example, as FAPO-11, FAPO-31 and so forth.

The term "essential empirical chemical composition" is meant to include the crystal framework and can include any organic templating agent present in the pore system, but does not include alkali metal or

other ions which can be present by virtue of ^" being contained in the reaction mixture or as a result of post-synthesis ion-exchange. Such ionic species, when present, function primarily as charge-balancing ions for Fe0 ₂ — and/or A10 ₂ —2 tetrahedra, Fe0 ₂ —2 tetrahedra associated with P0 ₂ tetrahedra or not associated with P0 ₂ tetrahedra or an organic ion derived from the organic templating agent.

The aforesaid ferroaluminophosphates are synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of iron oxide, alumina and phosphate, an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and optionally an alkali metal. The reaction mixture is placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetra¬ fluoroethylene and heated, preferably under autogenous pressure at a temperature of at least 100*C, and preferably between 100*C and 250*C, until crystals of the metal aluminophosphate product are obtained, usually a period of from 2 hours to 2 weeks. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the FAPO compositions, it is

— ^■ 1-JO- preferred to employ a reaction mixture composition expressed in terms of molar 'ratios as follows: aR : (Fe _χ Al _y P _z )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" has a value great enough to constitute an effective concentration of "R" and is within the range of >0 to 6;

"b" has a value of from zero to 500, preferably 2 to 80;

"x", "y" and "z" represent the mole fractions, respectively, of iron, aluminum and phosphorus in the

(FexAlyPJz 02« constituent, and each has a value of at least 0.01, and representing the following values for "x", "y" and "z": ole ac o

Point E

F

G

H

I J

In the foregoing expression of the reaction composition, the reactants are normalized with respect to a total of (Fe + Al + P) = (x + y + z) = 1.00 mole.

In forming the reaction mixture from which the ferroaluminophosphates are crystallized, the organic templating agent can be any of those heretofore proposed

for use in the synthesis of conventional zeolite aluminosilicates and micropdrous aluminophosphates. In general these compounds contain elements of Group VA of the Periodic Table of Elements, particularly nitrogen, phosphorus, arsenic and antimony, preferably N or P and most preferably N, which compounds also contain at least one alkyl or aryl group having from 1 to 8 carbon atoms. Particularly preferred nitrogen-containing compounds for use as templating agents are the amines and quaternary ammonium compounds, the latter being represented generally by the formula R ₄ N wherein each R is an alkyl or aryl group containing from 1 to 8 carbon atoms. Polymeric quaternary ammonium salts such as [(C ₁₄ H ₃₂ N ₂ ) ( H) ₂ ] _χ wherein "x" has a value of at least 2 are also suitably employed. Mono-, di- and triamines are advantageously utilized, either alone or in combination with a quaternary ammonium compound or other templating compound. Mixtures of two or more templating agents can either produce mixtures of the desired metal aluminophosphates or the more strongly directing templating species may control the course of the reaction with the other templating species serving primarily to establish the pH conditions of the reaction gel. Representative templating agents include tetramethylammonium, tetraethylammonium, tetrapropylammonium or tetrabutylammonium ions;

di-n-propylamine; tri-n-propylamine; triethylamine; triethanolamine; piperidine,** cyclohexylamine; 2-methylpyridine; N,N-dimethylbenzylamine; N-N-dimethylethanolamine; choline; N,N'-dimethylpiperazine; 1,4-diazabicyclo (2,2,2) octane; N-methyldiethanolamine; N-methylethanolamine; N-methylpiperidine; 3-methylpiperidine; N-methylcyclohexylamine; 3-methylpyridine; 4-methylpyridine; quinuclidine; N,N'-dimethyl-l,4-diazabicyclo (2,2,2) octane ion; di-n-butylamine; neopentylamine; di-n-pentylamine; isopropylamine; t-butylamine; ethylenediamine; pyrrolidine; and 2-imidazolidone. Not every templating agent will direct the formation of every species of ferroaluminophosphate (FAPO), i.e., a single templating agent can, with proper manipulation of the reaction conditions, direct the formation of several FAPO compositions, and a given FAPO composition can be produced using several different templating agents. The phosphorus source is preferably phosphoric acid, but organic phosphates such as triethylphosphate have been found satisfactory, and so also have crystalline or amorphous aluminophosphates such as the A1P0 ₄ composition of U.S. Patent No. 4,310,440. Organo-phosphorus compounds, such as tetrabutyl- phosphonium bromide do not, apparently serve as reactive

sources of phosphorus, but these compounds do function as templating agents. Conventional phosphorus salts such as sodium metaphosphate, may be used, at least in part, as the phosphorus source, but are not preferred. The aluminum source is preferably either an aluminum alkoxide, such as aluminum isopropoxide, or pseudoboehmite. The crystalline or amorphous aluminophosphates which are a suitable source of phosphorus are, of course, also suitable sources of aluminum. Other, sources of aluminum used in zeolite synthesis, such as gibbsite, sodium alu inate and aluminum trichloride, can be employed but are not preferred.

Iron can be introduced into the reaction system in any form which permits the formation in situ of reactive ferrous or ferric ions. Advantageously iron salts, oxides or hydroxides are employed such as iron sulfate, iron acetate, iron nitrate, or the like. Other sources such as a freshly precipitated iron oxide τ-FeOOH, are also suitable.

While not essential to the synthesis of FAPO compositions, it has been found that in general, stirring or other moderate agitation of the reaction mixture and/or seeding the reaction mixture with seed crystals of either the FAPO species to be produced or a topologically similar aluminophosphate or

aluminosilicate composition, facilitates the crystallization procedure.

After crystallization the FAPO product is isolated and advantageously washed with water and dried in air. The as-synthesized FAPO contains within its internal pore system at least one form of the templating agent employed in its formation. Most commonly the organic moiety is present, at least in part, as a charge-balancing cation as is generally the case with as-synthesized aluminosilicate zeolites prepared from organic-containing reaction systems. It is possible, however, that some or all of the organic moiety is an occluded molecular species in a particular FAPO species. As a general rule, the templating agent, and hence the occluded organic species, is too large to move freely through the pore system of the FAPO product and must be removed by calcining the FAPO at temperatures of 200 ^β C to 700*C to thermally degrade the organic species. In a few instances the pores of the FAPO product are sufficiently large to permit transport of the templating agent, particularly if the latter is a small molecule, and accordingly complete or partial removal thereof can be accomplished by conventional desorption procedures such as carried out in the case of zeolites. It will be - understood that the term "as-synthesized" as used herein and in the claims does not include the condition of the

FAPO phase wherein the organic moiety occupying the intracrystalline pore system as a result of the hydrothermal crystallization process has been reduced by post-synthesis treatment such that the value of "m" in the composition formula: mR : (Fe _χ Al _y P ₂ )0 ₂ has a value of less than 0.02. The other symbols of the formula are as defined hereinabove. In those preparations in which an aluminum alkoxide is employed as the source of aluminum, the corresponding alcohol is necessarily present in the reaction mixture since it is a hydrolysis product of the alkoxide. It has not been determined whether this alcohol participates in the syntheses process as a templating agent. For the purposes of this application, however, this alcohol is arbitrarily omitted from the class of templating agents, even if it is present in the as-synthesized FAPO material.

Since the FAPO compositions are formed from A10 ₂ —, P0 ₂ +, Fe0 ₂ — and/or Fe0 ₂ —2 units the matter of cation exchangeability is considerably more complicated than in the case of zeolitic molecular sieves in which, ideally, there is a stoichiometric relationship between

A10 ₂ tetrahedra and charge-balancing cations. In the FAPO compositions, an A10 ~ tetrahedron can be balanced electrically either by association with a P0 ₂

tetrahedron or a simple cation such as an alkali metal cation, a Fe +2 or Fe+3 cation present the reaction mixture, or an organic cation derived from the templating agent. Similarly an FeO_ — or FeO,—2

tetrahedron can be balanced electrically by association with P0 ₂ tetrahedron, a Fe or Fe cation, organic cations derived from the templating agent, or other metal cation introduced from an extraneous source. It has also been postulated that non-adjacent A10 ~ and P0 ₂ tetrahedral pairs can be balanced by Na and OH~, respectively [Flanigen and Grose, Molecular Sieve

Zeolites-I, ACS, Washington, D.C. (1971)].

TAPO MOLECULAR SIEVES

TAPO molecular sieves are disclosed in U.S. Patent No. 4,500,561, incorporated herein by reference, and comprise a three-dimensional microporous crystal framework structure of Ti0 ₂ , A10 ~ and 0 ₂ ⁺ tetrahedral units which has a unit empirical formula on an anhydrous basis of: mR : (Ti _χ Al _y P ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the moles of "R" present per mole of

(TixAlyPz)02_ and has a value of between zero and about 5.0, the maximum value in each case depending upon the molecular dimensions of the templating agent and the

available void volume of pore system of the particular titanium molecular sieve; "x", "y" and "z" represent the mole fractions of titanium, aluminum and phosphorus, respectively, present as tetrahedral oxides, representing the following values for "x", "y" and "z":

Mole ac

Point A B C

D

E

The parameters "x", "y" and "z" are preferably within the following values for "x", "y" and "z":

Point a b c d e

The titanium-containing molecular sieves are referred to hereinafter, solely for point of reference herein as "TAPO" molecular sieves, or as "TAPOs" if the reference is to the class as a whole. This designation is simply made for the sake of convenient reference

herein and is not meant to designate a particular structure for any given TAPO molecular sieve. The members of the class of TAPO's employed hereinafter in the examples will be characterized simply by referring to such members as TAPO-5, TAPO-11, etc, i.e., a particular species will be referred to as TAPO-n where "n" is a number specific to a given class member as its preparation is reported herein. This designation is an arbitrary one and is not intended to denote structural relationship to another material(s) which may also be characterized by a numbering system.

The term "unit empirical formula" is used herein according to its common meaning to designate the simplest formula which gives the relative number of moles of titanium, aluminum and phosphorus which form the [Ti0 ₂ ], [P0 and [A10 ₂ ] tetrahedral unit within a titanium-containing molecular sieve and which forms the molecular framework of the TAPO composition(s) . The unit empirical formula is given in terms of titanium, aluminum and phosphorus as shown in Formula (1) , above, and does not include other compounds, cations or anions which may be present as a result of the preparation or the existence of other impurities or materials in the bulk composition not containing the aforementioned tetrahedral unit. The amount of template R is reported as part of the composition when the as-synthesized unit

empirical ^" formula is given, and water may also be reported unless such is defined as the anhydrous form. For convenience, coefficient "m" for template "R" is reported as a value that is normalized by dividing the number of moles of organic templating agent by the total moles of titanium, aluminum and phosphorus.

The. unit empirical formula for a TAPO may be given on an "as-syrithesized" basis or may be given after an "as-synthesized" TAPO composition has been subjected to some post treatment process, e.g., calcination. The term "as-synthesized" herein shall be used to refer to the TAPO composition(s) formed as a result of the hydrothermal crystallization but before the TAPO composition has been subjected to post treatment to remove any volatile components present therein. The actual value of "m" for a post-treated TAPO will depend on several factors (including: the particular TAPO, template, severity of the post-treatment in terms of its ability to remove the template from the TAPO, the proposed application of the TAPO composition, and etc.) and the value for "m" can be within the range of values as defined for the as-synthesized TAPO compositions although such is generally less than the as-synthesized TAPO unless such post-treatment process, adds template to the TAPO so treated. A TAPO composition which is in the calcined or other post-treatment form generally has an

empirical formula represented by Formula (1) , except that the value of "m" is ^" generally less than about 0.02. Under sufficiently severe post-treatment conditions, e.g., roasting in air at high temperature for long. periods (over 1 hr.), the value of "m" may be zero (0) or, in any event, the template, R, is undetectable by normal analytical procedures.

The TAPO ^" molecular sieves are generally further characterized by an intracrystalline adsorption capacity for water at 4.6 torr and about 24 ^β C of about 3.0 weight percent. The adsorption of water has been observed to be completely reversible while retaining the same essential framework topology in both the hydrated and dehydrated state. The term "essential framework topology" is meant to designate the spatial arrangement of the primary bond linkages. A lack of change in the framework topology indicates that there is no disruption of these primary bond linkages.

The TAPO molecular sieves are generally synthesized by hydrothermal crystallization from a reaction mixture comprising reactive sources of titanium, aluminum and phosphorus, and one or more organic templating agents. Optionally, alkali metal(s) may be present in the reaction mixture. The reaction mixture is placed in a pressure vessel, preferably lined with an inert plastic material, such as polytetra-

fluoroethylene, and heated, preferably under autogenous pressure, at a temperature of at least about 100 ^β C, and preferably between 100 ^β C and 250"C, until crystals of the molecular sieve product are obtained, usually for a period of from 2 hours to 2 weeks. While not essential to the synthesis of the TAPO molecular sieves, it has been found that in general stirring or other moderate agitation of the reaction mixture and/or seeding the reaction mixture with seed crystals of either the TAPO to be produced, or a topologically similar composition, facilitates the crystallization procedure. The product is recovered by any convenient method such as centrifugation or filtration.

After .crystallization the TAPO(s) may be isolated and washed with water and dried in air. As a result of the hydrothermal crystallization, the as-synthesized TAPO contains within its intracrystalline pore system at least one form of the template employed in -its formation. Generally, the template is a molecular species, but it is possible, steric considerations permitting, that at least some of the template is present as a charge-balancing cation. Generally -the template is too large to move freely through the intracrystalline pore system of the formed TAPO and may be removed by a post-treatment process, such as by calcining the TAPO at temperatures of between

about 200 ^β C and to about 700"C so as to thermally degrade the template or by employing some other post-treatment process for removal of at least part of the template from the TAPO. In some instances the pores of the TAPO are sufficiently large to permit transport of the template, and, accordingly, complete or partial removal thereof can be accomplished by conventional desorption procedures such as carried out in the case of zeolites. The TAPOs are preferably formed from a reaction mixture having a mole fraction of alkali metal cation which is sufficiently low that it does not interfere with the formation of the TAPO composition. The TAPO compositions are generally formed from a reaction mixture containing reactive sources of Ti0 ₂ , Al-O-, and ,O _g and an organic templating agent, said reaction mixture comprising a composition expressed in terms of molar oxide ratios of: fR ₂ 0 : (Ti _χ Al _y P ₂ )0 ₂ : g H.,0 wherein "R" is an organic templating agent; "f" has a value large enough to constitute an effective amount of "R", said effective amount being that amount which form said TAPO compositions; "g" has a value of from zero to 500; "x", "y" and "z" represent the mole fractions, respectively of titanium, aluminum and phosphorus iri the (Ti Al P )0, constituent, and each has a value of at

least 0.001 and being ^" within the following values for

Although the TAPO compositions will form if higher concentrations of alkali metal cation are present, such reaction mixtures are not generally preferred. A reaction mixture, expressed in terms of molar oxide ratios, comprising the following bulk composition is preferred: oR 2-0 : wM2,0 : (TiXAlyPz O2. : nH2.O• wherein "R" is an organic template; "o" has a value great enough to constitute an effective concentration of "R" and is preferably within the range of from greater than zero (0) to about 5.0; "M" is an alkali metal cation; "w" has a value of from zero to 2.5; "n" has a value between about zero (0) and about 500; "x", "y" and "z" represent the mole fractions, respectively, of titanium, aluminum and phosphorus in the (Ti Al P 0, constituent, and each has a value of at least 0.001 and being within the following values for "x", "y" and "z":

Point h

1 j k

When the TAPOs are synthesized by this method the value of "m" iri Formula (1) is generally above about 0.02. Though the presence of alkali metal cations is not preferred, when they are present in the reaction mixture it is preferred to first admix at least a portion (e.g., at least about 10 weight percent) of each of the aluminum and phosphorus sources in the substantial absence (e.g., preferably less than about 20 percent of the total weight of the aluminum source and phosphorus source) of the titanium source. This procedure avoids adding the phosphorus source to a basic reaction mixture containing the titanium source and aluminum source, (as was done in most of the published attempts to substitute isomorphously [ 0 ₂ 3 tetrahedra for [SiO tetrahedra in zeolitic structures) . Although the reaction mechanism is by no means clear at this time, the function of the template may be to favor the incorporation of [PO and [A10 tetrahedra in the framework structures of the crystalline products with

[TiO_] tetrahedra iso orphously replacing [PO_] tetrahedra.

The reaction mixture from which these TAPOs are formed contains one or more organic templating agents (templates) which can be most any of those heretofore proposed for use in the synthesis of aluminosilicates and aluminophosphates. The template preferably contains at least one element of Group VA of the Periodic Table, particularly nitrogen, phosphorus, arsenic and/or antimony, more preferably nitrogen or phosphorus and most preferably nitrogen and is desirably of the formula R ₄ wherein X is selected from the group consisting of nitrogen, phosphorus, arsenic and/or antimony and R may be hydrogen, alkyl, aryl, aralkyl, or aikylaryl group and is preferably aryl or alkyl containing between 1 and 8 carbon atoms, although more than eight carbon atoms may be present in the group "R" of the template. Nitrogen-containing templates are preferred, including amines and quaternary ammonium compounds, the latter being represented generally by the formula R' ₄ N wherein each R ¹ is an alkyl, aryl, aikylaryl, or aralkyl group; wherein R ¹ preferably contains from 1 to 8 carbon atoms or higher when R* is alkyl and greater than 6 carbon atoms when R ¹ is otherwise, as hereinbefore discussed. Polymeric quaternary ammonium salts such as [ ( _A ^H 3 ^N ) ( ^OH ) 2 - _K

wherein "x" has a value of at least 2 may also be employed. The mono-, di- and triamines, including mixed amines, may also be employed as templates either alone or in combination with a quaternary ammonium compound or another template. The exact relationship of various templates when concurrently employed is not clearly understood. Mixtures of two or more templating agents can produce either mixtures of TAPOs or in the instance where one template is more strongly directing than another template the more strongly directing template may control the course of the hydrothermal crystallization wherein with the other template serving primarily to establish the pH conditions of the reaction mixture. Representative templates include tetramethy1ammonium, tetraethylammonium, tetrapropylammonium or tetrabutylammonium ions; di-n-propylamine; tripropylamine; triethylamine; triethanolamine; piperidine; cyclohexylamine; 2-methylpyridine; ,N-dimethylbenzylamine; N,N-diethylethanolamine; dicyclohexylamine; N,N-dimethylethanolamine; 1,4-diazabicyclo (2,2,2) octane; N-methyldiethanolamine, N-methyl-ethanolamine; N-methylcyclohexylamine; 3-methyl-pyridine; 4-methylpyridine; quinuclidine;

N,N--dimethyl-l,4-diazabicyclo (2,2,2) octane ion;

di-n-butylamine; neopentylamine; di-n-pentylamine; isopropylamine; t-butylamine; ethylenediamine; pyrrolidine; and 2-imidazolidone. Not every template will produce every TAPO composition although a single template can, with proper selection of the reaction conditions, cause the formation of different TAPO compositions,, and a given TAPO composition can be produced using different templates.

In those instances where an aluminum alkoxide is the reactive aluminum source, the corresponding alcohol is necessarily present in the reaction mixture since it is a hydrolysis product of the alkoxide. It has not as yet been determined whether this alcohol participates in the synthesis process as a templating agent, or in some other function and, accordingly, is not reported as a template in the unit formula of the TAPOs, although such may be acting as templates.

Alkali metal cations, if present in the reaction mixture, may facilitate the crystallization of certain TAPO phases, although the exact function of such cations, when present, in crystallization, if any, is not presently known. Alkali cations present in the reaction mixture generally appear in the formed TAPO composition, either as occluded (extraneous) cations and/or as structural cations balancing net negative charges at various sites in the crystal lattice. It

should be understood that although the unit formula for the TAPOs does not specifically recite the presence of alkali cations they are not excluded in the same sense that hydrogen cations and/or hydroxyl groups are not specifically provided for in the traditional formulae for zeolitic aluminosilicates.

Almost any reactive titanium source may be employed herein. The preferred reactive titanium sources include titanium alkoxides, water-soluble titanates and titanium chelates.

Almost any reactive phosphorus source may be employed. Phosphoric acid is the most suitable phosphorus source employed to date. Accordingly, other acids of phosphorus are generally believed to be suitable phosphorus sources for use herein. Organic phosphates such as triethyl phosphate have been found satisfactory, and so also have crystalline or amorphous aluminophosphates such as the A1P0 ₄ compositions of U.S. Patent 4,310,440. Organo-phosphorus compounds, such as tetrabutyl-phosphonium bromide have not, apparently, served as reactive sources of phosphorus, but these compounds do function as templating agents and may also be capable of being suitable phosphorus sources under proper process conditions (yet to be ascertained) . Organic phosphorus compounds, e.g., esters, are believed to be generally suitable since they can generate acids

of phosphorus in situ. Conventional phosphorus salts, such as sodium metaphosphate, may be used, at least in part as the phosphorus source, but they are not preferred. Almost any reactive aluminum source may be employed herein. The preferred reactive aluminum sources include aluminum alkoxides, such as aluminum isopropoxide, and pseudoboehmite. Crystalline or amorphous aluminophosphates which are a suitable source of phosphorus are, of course, also suitable sources of aluminum. Other sources of aluminum used in zeolite synthesis, such as gibbsite, sodium aluminate and aluminum trichloride, can be employed but as generally not preferred. Since the exact nature of the TAPO molecular sieves are not clearly understood at present, although all are believed to contain [TiO tetrahedra in the three-dimensional microporous crystal framework structure, it is advantageous to characterize the TAPO molecular sieves by means of their chemical composition. This is due to the low level of titanium present in certain of the TAPO molecular sieves prepared to date which makes it difficult to ascertain the exact nature of the interaction between titanium, aluminum and phosphorus. As a result, although it is believed that titanium, [TiO_], has substituted isomorphously for

[A10 or [P0 ₂ ] tetrahedra, it is appropriate to characterize certain TAPO compositions by reference to their chemical composition in terms of the mole ratios of oxides in the as-synthesized and anhydrous form as: vR : p i0 ₂ : qAl ₂ 0 ₃ : P ₂ 0_ wherein "R" represents at least one organic templating agent present- in the intracrystalline pore system; "v" represents an effective amount of the organic templating agent to form said TAPO compositions and preferably has a value between and including zero and about 3.0; "p", "q" and "r" represent moles, respectively, of titanium, alumina and phosphorus pentoxide, based on said moles being such that they are within the following values for "p", "q" and "r":

Point A B C D E The parameters "p", "q" and "r" are preferably within the following values for "p", "q" and "r":

-155-

Point a b c d e

"ELAPO" molecular sieves are a class of crystalline molecular sieves in which at least one element capable of forming a three-dimensional microporous framework forms crystal framework structures of A10 ^' P0 ₂ and 0 ₂ ⁿ tetrahedral oxide units wherein

"MO.n," represents at least one different element (other than Al or P) present as tetrahedral oxide units "M0 ₂ ⁿ " with charge "n" where "n" may be -3, -2, -1, 0 or +1. The members of this novel class of molecular sieve compositions have crystal framework structures of A10 ~, P0 ₂ ⁺ and M0 ₂ ⁿ tetrahedral units and have an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (M _χ Al _y P ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of (M Al P )0,; "M" represents at least one element capable

of forming framework tetrahedral oxides; and "x", "y" and "z" represent the mole fractions of "M", aluminum and phosphorus, respectively, present as tetrahedral oxides. "M" is at least one different (i^e., not aluminum, phosphorus or oxygen) element such that the molecular sieves contain at least one framework tetrahedral unit in addition to A10 ~ and P0 ₂ . "M" is at least one element selected from the group consisting of arsenic, beryllium, boron, cobalt, chromium, gallium, germanium, iron, lithium, magnesium, manganese, titanium and zinc, subject to certain restrictions on the combinations of elements as will appear from the discussions of individual groups of ELAPOs below. ELAPOs and their preparation are disclosed in European Patent Application Serial No. 85104386.9, filed April

11, 1985 (EPC Publication No. 0158976, published October 13, 1985, incorporated herein by reference) and 85104388.5, filed April 11, 1985 (EPC Publication No. 158349, published October 16, 1985, incorporated herein by reference) .

The "ELAPO" molecular sieves further include numerous species which are intended herein to be within the scope of the term "non-zeolitic molecular sieves" such being disclosed in the following copending and commonly assigned applications, incorporated herein by reference thereto [ (A) following a serial number

indicates that the application is abandoned, while (CIP) following a serial number indicates that ^" the application is a continuation-in-part of the immediately preceding application, and (C) indicates that the application is a continuation of the immediately preceding application] :

U.S. Serial No. Filed NZMS 600, 166(A) April 13, -1984 ASAPO 830,889(CIP) Feb. 19, 1986 AsAPO 599,812 (A) April 13, 1984 BAPO 804,248(C) (A) Dec. 4, 1985 BAPO 29,540(CIP) March 24, 1987 BAPO 599,776(A) April 13, 1984 BeAPO 835,293(CIP) March 3, 1986 BeAPO 599,813 (A) April 13, 1984 CAPO 830,756(CIP) Feb. 19, 1986 CAPO 599,771(A) April 13, 1984 GaAPO 830,890(CIP) Feb. 19, 1986 GaAPO 599,807 (A) April 13, 1984 GeAPO 841,753 (CIP) March 20, 1986 GeAPO 599,811(A) April 13, 1984 LiAPO 834,921(CIP) Feb. 28, 1986 LiAPO 600,171 April 13, 1984 FCAPO

(now U.S. Patent No. 4,686,093 issued August 11, 1987)

600,172 (A) April 13, 1984 ) E1APO (M

) comprises two

) different

846.088 (CIP) March 31, 1986 ) elements) 599,824(A) April 13, 1984 FeTiAPO 902,129(C) September 2, 1986 FeTiAPO 599,810(A) April 13, 1984 XAPO 902, 020(C) September 2, 1986 XAPO The ELAPO molecular sieves are generally referred to herein by the acronym "ELAPO" to designate

-ISO- element(s) "M" in a framework of AIO ~, P0 ₂ ⁺ and MO ⁿ tetrahedral oxide units. Actual class members will be identified by replacing the "EL" of the acronym with the elements present as MO- ⁿ tetrahedral units. For example, "MgBeAPO" designates a molecular sieve comprised of A10 ₂ —, P0 ₂ •+*, Mg0 ₂ —2 and Be0 ₂ —2 tetrahedral units. To identify various structural species which make up each of the subgeneric classes, each species is assigned a number and is identified as "ELAPO-i" wherein "i" is an integer. The given species designation is not intended to denote a similarity in structure to any other species denominated by a similar identification system.

The ELAPO molecular sieves comprise at least one additional element capable of forming framework tetrahedral oxide units (M0 ₂ ⁿ ) to form crystal framework structures with A10 ₂ ~ and P0 ₂ tetrahedral oxide units wherein "M" represents at least one element capable of- forming tetrahedral units "MO^" where "n" is -3, -2, -1, 0 or ÷l and is at least one element selected from the group consisting of arsenic, beryllium, boron, cobalt, chromium, gallium, germanium, iron, lithium, magnesium, manganese, titanium and zinc.

The ELAPO molecular sieves have crystalline three-dimensional microporous framework structures of AIO ~, P0 ₂ ⁺ and M0 ₂ ⁿ tetrahedral units and have an

empirical chemical composition on an anhydrous basis expressed by the formula: mR : (M _χ Al _y P ₂ )0 ₂ ; wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of (M XAI %P Z 04,b and has a value of zero to about 0.3; "M" represents at least one element capable of forming framework tetrahedral oxides where "M" is at least one element selected from the group consisting of arsenic, beryllium, boron, cobalt, chromium, gallium, germanium, iron, lithium, magnesium, manganese, titanium and zinc.

The relative amounts of element(s) "M", aluminum and phosphorus are expressed by the empirical chemical formula (anhydrous) : mR : (M _χ Al _y P ₂ )0 ₂ where "x", "y" and ^■■ z" represent the mole fractions of said "M", aluminum and phosphorus. The individual mole fractions of each ^,, M" (or when M denotes two or more elements, M-, M ₂ , M ₃ , etc.) may be represented by "x,", "x ₂ ", "x ₃ ", etc. wherein "x^ ¹ , "x ₂ ", and ^» x ₃ " etc. represent the individual mole fractions of elements M., ₂ , M ₃ , and etc. for "M" as above defined. The values of "x^ ¹ , "x^ ¹ , "x ₃ " etc. are as defined for "x", hereinafter, where "x " + "x ₂ " + "x ₃ " . . . = "x" and where x., x ₂ , x ₃ , etc. are each at least 0.01.

The ELAPO molecular sieves have crystalline three-dimensional microporous framework structures ^" of

M0 ₂ ⁿ , A10 ~ and P0 ₂ tetrahedral units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (M _χ Al _y P _z )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents a molar amount of "R" present per mole of (M„xA1„yP„z)'0.2 and has a value of zero to about 0.3; "M" represents at least one different element (other than Al or P) capable of forming framework tetrahedral oxides, as hereinbefore defined, and "x", "y" and "z" represent the mole fractions of "M", aluminum and phosphorus, respectively, present as tetrahedral oxides; in general, said mole fractions "x", "y" and "z" are within the following values for "x", "y" and "z", although as will appear hereinbelow, the limits for "x", "y" and "z" may vary slightly with the nature of the element "M": Mole Fraction

Point x X J_L

A 0.02 0.60 0.38

B 0.02 0.38 0.60

C 0.39 0.01 0.60 D 0.98 0.01 0.01

E 0.39 0.60 0.01

Also, in general, in a preferred sub-class of the ELAPOs of this invention, the values of "x", "y" and "z" in the formula above are within the following values for "x", "y" and "z", although again the relevant limits may vary somewhat with the nature of the element "M", as set forth hereinbelow:

Mole Fract on

ELAPO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of the elements "M", aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably ' a compound of an element of Group VA of the Periodic

Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed iri a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between 50 ^β C and 250'C, and preferably between 100 ^β C and

200 ° C, until crystals of the ELAPO product are obtained, usually a period of from several hours to ^" several weeks. Typical crystallization times are from about 2 hours to about 30 days with from about 2 hours to about 20 days being generally employed to obtain crystals of the ELAPO products. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the ELAPO compositions of the instant invention, it is in general preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (M _χ Al _y P ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6; "b" has a value of from zero (0) to about 500, preferably between about 2 and 300; "M" represents at least one element, as above described, capable of forming tetrahedral oxide framework units, M0 ₂ ⁿ , with

AIO ~ and P0 ₂ tetrahedral units; "n" has a value of -3, -2, -1, 0 or +1; and "x", "y" and "z" represent the mole fractions of "M", aluminum and phosphorus, respectively; "y" and "z" each have a value of at least 0.01 and "x" has a value of at least 0.01 with each element "M" having a mole fraction of at least 0.01. In general,

the mole fractions "x", "y" and "z" are preferably within the following values -for "x", "y" and "z":

Mo act Point F G H I J Further guidance concerning the preferred reaction mixtures for forming ELAPOs with various elements "M" will be given below.

In the foregoing expression of the reaction composition, the reactants are normalized with respect to a total of (M + Al + P) = (x + y + z) = 1.00 mole, whereas in other cases the reaction mixtures are expressed in terms of molar oxide ratios and may be normalized to 1.00 mole of P ₂ 0 _ς and/or 1 ₂ 0 ₃ . This latter form is readily converted to the former form by routine calculations by dividing the total number of moles of "M", aluminum and phosphorus into the moles of each of "M", aluminum and phosphorus. The moles of template and water are similarly normalized by dividing by the total moles of "M", aluminum and phosphorus. In forming the reaction mixture from which the instant molecular sieves are formed the organic

templating agent can be any of those heretofore proposed for use in the synthesis of-conventional zeolite ^" aluminosilicates. In general these compounds contain elements of Group VA of the Periodic Table of Elements, particularly nitrogen, phosphorus, arsenic and antimony, preferably nitrogen or phosphorus and most preferably nitrogen, which compounds also contain at least one alkyl or aryl group having from 1 to 8 carbon atoms. Particularly preferred compounds for use as templating agents are the amines, quaternary phosphonium compounds and quaternary ammonium compounds, the latter two being represented generally by the formula R ₄ X wherein "X" is nitrogen or phosphorus and each R is an alkyl or aryl group containing from 1 to 8 carbon atoms. Polymeric quaternary ammonium salts such as C( ₁₄ ^H ₃₂ ^N ₂ *' ^ ^0H - ¹ ₂ -- _X wherein "x" has a value of at least 2 are also suitably employed. The mono-, di- and tri-amines are advantageously utilized, either alone or in combination with a quaternary ammonium compound or other templating compound. Mixtures of two or more templating agents can either produce mixtures of the desired ELAPOs or the more strongly directing templating species may control the course of the reaction with the other templating species serving primarily to establish the pH conditions of the reaction gel. Representative templating agents include tetramethylammonium, tetraethylammonium.

tεtrapropylammonium or tetrabutylammonium ions; tetrapentylammonium ion; di-n-propylamine; tripropylamine; triethylamine; triethanolamine; piperidine; cyclohexyla ine; 2-methylpyridine; N,N-dimethylbenzylamine; N,N-dimethylethanolamine; choline; N,N ^• -dimethylpiperazine; 1,4-diazabicyclo (2,2,2,) octane; N-methyldiethanolamine;

N-methylethanolamine; N-methylpiperidine;

3-methylpiperidine; N-methylcyclohexylamine; 3-methylpyridine; 4-methylpyridine; quinuclidine;

N,N'-dimethyl-l,4-diazabicyclo (2,2,2) octane ion; di-n-butylamine, neopentylamine; di-n-pentylamine; isopropylamine; t-butylamine; ethylenediamine; pyrrolidine; and 2-imidazolidone. Not every templating agent will direct the formation of every species of

ELAPO, i.e., a single templating agent can, with proper manipulation of the reaction conditions, direct the formation of several ELAPO compositions, and a given

ELAPO composition can be produced using several different templating agents. The phosphorus source is preferably phosphoric acid, but organic phosphates such as triethyl phosphate may be satisfactory, and so also may crystalline or amorphous aluminophosphates such as the A1P0 ₄ composition of. U.S.P. 4,310,440. Organo- phosphorus compounds, such as tetrabutylphosphonium bromide, do not apparently serve as reactive sources of

phcsphorus, but these compounds may function as templating agents. Conventional phosphorus salts such as sodium metaphosphate, may be used, at least in part, as the phosphorus source, but are not preferred. The aluminum source is preferably either an aluminum alkoxide, such as aluminum isopropoxide, or pseudoboehmite. The crystalline or amorphous aluminophosphates which are a suitable source of phosphorus are, of course, also suitable sources of aluminum. Other sources of aluminum used in zeolite synthesis, such as gibbsite, sodium aluminate and aluminum trichloride, can be employed but are not preferred.

The element(s) "M" can be introduced into the reaction system in any form which permits the formation in situ of reactive form of the element, i.e., reactive to form the framework tetrahedral oxide unit of the element. The organic and inorganic salts, of "M" such as oxides, alkoxides, hydroxides, halides and carboxylates, may be employed including the chlorides, bromides, iodides, nitrates, sulfates, phosphates, acetates, formates, and alkoxides, including ethoxides, propoxides and the like. Specific preferred reagents for introducing various elements "M" are discussed hereinbelow.

While not essential to the synthesis of ELAPO compositions, stirring or other moderate agitation of the reaction mixture and/or seeding the reaction mixture with seed crystals of either the ELAPO species to be produced or a topologically similar species, such as aluminophosphate, alumino-silicate or molecular sieve compositions, ^• facilitates the crystallization procedure. After crystallization the ELAPO product may be isolated and advantageously washed with water and dried in air. The as-synthesized ELAPO generally contains within its internal pore system at least one form of the templating agent employed in its formation. Most commonly the organic moiety is present, at least in part, as a charge-balancing cation as is generally the case with as-synthesized aluminosilicate zeolites prepared from organic-containing reaction systems. It is possible, however, that some or all of the organic moiety is an occluded molecular species in a particular ELAPO species. As a general rule the templating agent, and hence the occluded organic species, is too large to move freely through the pore system of the ELAPO product and must be removed by calcining the ELAPO at temperatures of 200*C to 700'C to thermally degrade the organic species. In a few instances the pores of the ELAPO product are sufficiently large to permit transport of the templating agent, particularly if the latter is a

small molecule, and accordingly complete or partial removal thereof can be accomplished by conventional desorption procedures such as carried out in the case of zeolites. It will be understood that the term "as-synthesized" as used herein does not include the condition of the ELAPO phase wherein the organic moiety occupying the- intracrystalline pore system as a result of the hydrothermal crystallization process has been reduced by post-synthesis treatment such that the value of "m" in the composition formula:

has a value of less than 0.02. The other symbols of the formula are as defined hereinabove. In those preparations in which an alkoxide is employed as the source of element "M", aluminum or phosphorus, the corresponding alcohol is necessarily present in the reaction mixture since it is a hydrolysis product of the alkoxide. It has not been determined whether this alcohol participates in the synthesis process as a templating agent. For the purposes of this application, however, this alcohol is arbitrarily omitted from the class of templating agents, even if it is present in the as-synthesized ELAPO material.

Since the present ELAPO compositions are formed from M0 ₂ ⁿ , A10 ~ and P0 ₂ tetrahedral oxide units which, respectively, have a net charge of "n", (where

"m" may be -3, -2, -1, 0 or +1), -1 and +1, the matter of cation exchangeability is considerably more complicated than in the case of zeolitic molecular sieves in which, ideally, there is a stoichiometric relationship between A10 ~ tetrahedra and charge-balancing cations. In the instant compositions, an A10 ~ tetrahedron can be balanced electrically either by association with a PO tetrahedron or a simple cation such as an alkali metal cation, a proton (H ) , a cation of "M" present in the reaction mixture, or an organic cation derived from the templating agent. Similarly an M0 ₂ ⁿ tetrahedron, where "n" is negative, can be balanced electrically by association with P0 ₂ tetrahedra, a cation of "M" present in the reaction mixture, organic cations derived from the templating agent, a simple cation such as an alkali metal cation, or other divalent or polyvalent metal cation, a proton (H ) , or anions or cations introduced from an extraneous source. It has also been postulated that non-adjacent AIO ~ and P0 ₂ tetrahedral pairs can be balanced by Na and OH respectively [Flanigen and Grose, Molecular Sieve Zeolites-I, ACS, Washington, DC ^' (1971) .

ASAPO MOLECULAR SIEVES The AsAPO molecular sieves of U.S. Serial No. 600,166, filed April 13, 1984, and U.S. Serial No. 830,889 filed February 19, 1986 have a framework

structure of As0 ₂ ⁿ , AIO ~ and P0 ₂ tetrahedral units

(where "n ^M is -1 or +1) and-have an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (As _χ Al _y P ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of ^■ *R" present per mole of

(As_x.A1„yPJz 02_ and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "x", "y" and "z" represent the mole fractions of the elements arsenic, aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows: . e Fract o Point A B C D E F

There are two preferred subclasses of the AsAPO molecular sieves, depending upon whether the value of "n" is -1 or +1 (i.e. whether the arsenic is

trivalent or pentavalent) , it being understood that mixtures of such are permitted in a given AsAPO. When ^" "n" is -1, the preferred values of x, y and z are within the limiting compositional values or points as follows: Mole Fraction

Point x X JL a 0.01 0.59 0.40 b 0.01 0.39 0.60 c 0.39 0.01 0.60 d 0.59 0.01 0.40

When "n" is +1, the preferred values of x, y and z are within the limiting compositional values or points as follows:

Point e f g h In an especially preferred subclass of the

AsAPO molecular sieves' in which "n" = +1, the values of x, y and z are as follows:

Point

3 k 1 m n

AsAPO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of arsenic, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element, of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50°C and about 250*C, and preferably between about 100*C and about 200'C until crystals of the AsAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 2 hours to about 20 days, and preferably about 12 hours to about 7 days,

have been observed. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the AsAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (As _χ Al _y P ₂ )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.5; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 20; and "x", "y" and "z" represent the mole fractions of arsenic, aluminum and phosphorus, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point G H I J K

Especially preferred reaction mixtures are those wherein the mole fractions "x", "y" and "z" are within the limiting compositional values or points as follows:

Point a b c d e f In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "x", "y" and "z ^l! such that (x + y + z) = 1.00 mole. Molecular sieves containing arsenic, aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

'— 1 " ^** "7 —

Preparative Reagents AsAPO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare AsAPOs include: (a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide; (c)' H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid; (d) As ₂ 0 ₅ , arsenic(V) oxide; (e) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(f) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(g) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH; (h) Pr ₃ N: tri-n-propylamine, (C ₃ H._) ₃ N;

(i) Quin: Quinuclidine, (C_H ₁₃ N) ;

(j) MQuin: Methyl Quinuclidine hydroxide,

(C ₇ H ₁₃ NCH ₃ OH) ; (k) C-hex: cyclohexylamine; (1) TMAOH: tetramethylammonium hydroxide;

(m) TPAOH: tetrapropylammonium hydroxide; and (n) DEEA: 2-diethylaminoethanol.

Preparative Procedures AsAPOs may be prepared by forming a starting reaction mixture by dissolving the arsenic(V) oxide and the H ₃ P0 ₄ in at least part of the water. To this

solution the aluminum oxide or isopropoxide is added. This mixture is then .blended until a homogeneous mixture is observed. To this mixture the templating agent and the resulting mixture blended until a homogeneous mixture is observed. The mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150'C or 200*C) for a time or placed in lined screw top bottles for digestion at 100"C. Digestions are typically carried out under autogenous pressure.

BAPO MOLECULAR SIEVES The BAPO molecular sieves of U.S. Serial No. 599,812, filed April 13, 1984, U.S. Serial No. 804,248, filed December 4, 1985, and U.S. Serial No. 29,540, filed March 24, 1987, have a framework structure of BO ~, AIO ~ and PO- tetrahedral units and have an empirical chemical composition on an anhydrous basis expressed by the formula:

wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(B Al PJO, and has a value of zero to about 0.3, "x",

"y" and "z" represent the mole fractions of the elements boron, aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and "z"

are generally defined as being within the limiting compositional values or points as follows:

Mo e F ac o

Point A

B

C

D

E F

In a preferred subclass of the BAPO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

Mo e F actio Point a b c d An especially preferred subclass of the BAPO molecular sieves are those in which the mole fraction, "x", of boron is not greater than about 0.3.

BAPO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of boron, aluminum and phosphorus, preferably an organic templating, i.e.,

structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50°C and about 250'C, and preferably between about 100*c and about 200"C until crystals of the BAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 14 days, and preferably about 1 to about 7 days, have been observed. The product is recovered by any convenient method such as centrifugation or ■ filtration.

In synthesizing the BAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (B _χ Al _y P ₂ )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and is an effective amount preferably within the range of greater than zero (0) to about 6, and most preferably not more than about 1.0; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, desirably not greater than about 20, and most desirably

-131- not greater than about 10; and "x", "y" and "z" represent the mole fractions of boron, aluminum and phosphorus, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z" are generally, defined as being within the limiting compositional values or points as follows:

Mole Fraction Point G H I J K

Especially preferred reaction mixtures are those containing from 0.5 to 2.0 moles of B 0 ₃ and from 0.75 to.1.25 moles of A1 ₂ 0 ₃ for each mole of P2θ5-

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "x", "y" and "z" such that (x + y + z) = 1.00 mole.

The exact nature of the BAPO molecular sieves is not entirely understood at present, although all are believed to contain B0 ₂ , A10 ₂ and P0 ₂ tetrahedra in the three-dimensional microporous framework structure. The

^• -132- low level of boron present in some of the instant molecular sieves makes it difficult to ascertain the exact nature of the interactions among boron, aluminum and phosphorus. As a result, although it is believed that B0 ₂ tetrahedra are present in the three-dimensional microporous framework structure, it is appropriate to characterize certain BAPO compositions in terms of the molar ratios of oxides.

Molecular sieves containing boron, aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents BAPO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare BAPOs include:

(a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide;

(c) H_P0 ₄ : 85 weight percent aqueous phosphoric acid; (d) boric acid or trimethylborate;

(e) TEAOH: 40 weight percent aqueous solution ^• of tetraethylammonium hydroxide;

(f) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (g) Pr ₂ NH: di-n-propylamine, (C ₃ H _? ) ₂ NH;

(h) Pr ₃ N: tri-n-propylamine, (C ₃ H ₇ ) ₃ ;

-133- (i) Quin: Quinuclidine. (C-H.-.N) ; (j) MQuin: Methyl Quinuclidine hydroxide,

^• (C ₇ H ₁₃ NCH ₃ OH) ; (k) C-hex: cyclohexylamine; (1) TMAOH: tetramethylammonium hydroxide;

(m) TPAOH: tetrapropylammonium hydroxide; and (n) - DEEA: 2-diethylaminoethanol.

Preparative Procedures In the preferred method of synthesizing the BAPO compositions, one first combines sources of boron, aluminum and phosphorus to form an amorphous material containing all three elements, and thereafter heats the amorphous material to produce a crystalline BAPO molecular sieve. It is not necessary that the total quantities of the reactive sources of boron, aluminum and phosphorus to be used in the final reaction mixture be present in the amorphous material, since additional quantities of the elements can be added during the later heat treatment; in particular, it has been found convenient to add additional quantities of phosphorus to the amorphous material before the heat treatment. The preliminary formation of the amorphous material assists in the incorporation of the boron into the final molecular sieve. For example, BAPOs may be prepared by forming a solution of boric acid in a methanolic solution of the

-134- templating agent, then adding a hydrated aluminophosphate and water and stirring to form a homogeneous reaction slurry. This slurry is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150°C or 200 ^β C) for a time or placed in lined screw top bottles for digestion at 100°C. Digestions are typically carried out under autogenous pressure.

BeAPO MOLECULAR SIEVES The BeAPO molecular sieves of U.S. Serial No.

599,776, filed April 13, 1984, and U.S. Serial No. 835,293 filed March 3, 1986 have a framework structure of Be0 ₂ —2, A10 ₂ — and P0 ₂ 4* tetrahedral units and have an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Be _χ Al _y P ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of (BexAly„PzJO«2 and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "x", "y" and "z" represent the mole fractions of the elements beryllium, aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point A B C

D E F

In a preferred subclass of the BeAPO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

Mole Fraction

Point x X z. a 0.01 0.60 0,39 b 0.01 0.39 0.60

C 0.35 0.05 0.60 d 0.35 0.60 0.05

In an especially preferred subclass of the BeAPO molecular sieves the values of x, y and z are as follows:

Mole Fraction Point x z. β 0.02 0.46 0.52 f 0.10 0.38 0.52 g OolO 0.46 0.44

-136- BeAPO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of beryllium, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an " element of Group VA of the Periodic Table, and/or optionally ari alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50"C and about 250*C, and preferably between about 100"C and about 200"C until crystals of the BeAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 14 days, and preferably about 1 to about 7 days, have been observed. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the BeAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Be _χ Al _y P ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective

amount within the ^" range of greater than zero (0) to about 6, and most preferably not more than about 1.5; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 50; and "x", "y" and "z" represent the mole fractions of beryllium, aluminum and phosphorus, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Fract o Point G H I J K Especially preferred reaction mixtures are those wherein the mole fractions "x", "y" and "z" are within the limiting compositional values or points as follows:

Point g h i j k

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "x", "y" and "z" such that

(x 4- y ^• + ^• z) = 1.00 mole. Molecular sieves containing beryllium, aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents BeAPO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare BeAPOs include:

(a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide; (c) H_P0 ₄ : 85 weight percent aqueous phosphoric acid;

(d) beryllium sulfate;

(e) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; (f) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

-139- (g) Pr ₂ NH: di-n-prbpylamine, (C ₃ H _? ) NH; (h) Pr ₃ N: tri-n-propylamine, (C ₃ H _? ) N; (i) Quin: Quinuclidine, (α_H ₁₃ N) ; (j) MQuin: Methyl Quinuclidine hydroxide, (C ₇ H ₁₃ NCH ₃ OH) ;

(k) C-hex: cyclohexylamine; (1) ^' TMAOH: tetramethylammonium hydroxide; (m) TPAOH: tetrapropylammonium hydroxide; and (n) DEEA: 2-diethylaminoethanol. Preparative Procedures

BeAPOs may be prepared by forming a starting reaction mixture by dissolving the beryllium sulfate and the H ₃ P0 ₄ in at least part of the water. To this solution the aluminum oxide or isopropoxide is added. This mixture is then blended until a homogeneous mixture is observed. To this mixture the templating agent and the resulting mixture blended until a homogeneous mixture is observed. The mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150"C or 200 ^β C) for a time or placed in lined screw top bottles for digestion at 100 ^β C. Digestions are typically carried out under autogenous pressure.

CAPO MOLECULAR SIEVES The CAPO molecular sieves of U.S. Serial No.

599,813, filed April 13, 1984, and U.S. Serial No.

830,756 filed February 19, 1986 have a framework structure of Cr0 ₂ ⁿ , AIO ~ and P0 ₂ tetrahedral units (where "n" is -1, 0 or 4-1) and have an empirical chemical composition on an anhydrous basis expressed by the formula:

^{' :} < ^Cr x ^A1 y ^P z ⁾⁰ 2 wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of (CrxAly.PzJO2- and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "x", "y" and "z" represent the mole fractions of the elements chromium, aluminum and phosphorus, respectively, present as tetrahedral oxides. When "n" is -1 or 4-1, the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point A

B C D Ξ F

When "n" is 0, the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole F action Point G H I J K

There are three preferred subclasses of the CAPO molecular sieves, depending upon whether the value of "n" is -1, 0 or 4-1 (i.e. whether the chromium has an oxidation number of 3, 4 or 5), it being understood that mixtures of such are. permitted in a given CAPO. When

"n" is -1, the preferred values of x, y and z are within the limiting compositional values or points as follows:

Mole Fraction

Point x y. _z a 0.01 0.59 0.40 b 0.01 0.39 0.60

C 0.39 0.01 0.60 d 0.59 0.01 0.40

In an especially preferred subclass of these CAPSO molecular sieves in which "n" = -1, the values of x, y and z are as follows:

Point n o p g r s When "n" is 0, the preferred values of x, y and z are within the limiting compositional values or points as follows:

Point e f g h

1

When "n" is 4-1, the preferred values of x, y and z are within the limiting compositional values or points as follows:

Point

_*

3 k 1 m

Since the exact nature of the CAPO molecular sieves is not clearly understood at present, altnough all are believed to contain Cr0 ₂ tetrahedra in the three-dimensional microporous crystal framework structure, it is advantageous to characterize the CAPO molecular sieves by means of their chemical composition. This is due to the low level of chromium present in certain of the CAPO molecular sieves prepared to date which makes it difficult to ascertain the exact nature of the interaction between chromium, aluminum and phosphorus. As a result, although it is believed that Cr0 ₂ tetrahedra are substituted isomorphously for A10 ₂ or PO- tetrahedra, it is appropriate to characterize certain CAPO compositions by reference to their chemical composition in terms of the mole ratios of oxides.

CAPO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of chromium, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an

element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50 ^β C and about 250*C, and preferably between about 100"C and about 200*C until crystals of the CAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 2 hours to about 20 days, and preferably about 1 to about 10 days, have been observed. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the CAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Cr _χ Al _y P ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.6; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 20; and "x", "y" and

"z" represent the mole fractions of chromium, aluminum and phosphorus, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Point L M N 0 P Especially preferred reaction mixtures are those containing from about 0.1 to about 0.4 moles of chromium, and from about 0.75 to about 1.25 moles of aluminum, per mole of phosphorus.

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "x", "y" and ^» z" such that (x 4- y 4- z) = 1.00 mole. Molecular sieves containing chromium, aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents CAPO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare CAPOs include: (a) aluminum isopropoxide, or aluminum chlorhydrol;

(b) pseudoboehmite or other aluminum oxide;

(c) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid; (d) chromium(III) orthophosphate, chromium(III) acetate and chromium acetate hydroxide, (Cr ₃ (OH) ₂ (CH ₃ COO) _? );

(e) TEAOH: 40 weight percent aqueous solution of.tetraethylammonium hydroxide;

(f) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(g) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH; (h) Pr ₃ N: tri-n-propylamine, (C ₃ H ₇ ) ₃ ; (i) Quin: Quinuclidine, (C ₇ H_ ₃ N) ;

(j) MQuin: Methyl Quinuclidine hydroxide, (C _y H ₁₃ NCH ₃ OH) ;

(k) C-hex: cyclohexylamine;

(1) TMAOH: tetramethylammonium hydroxide; (m) TPAOH: tetrapropylammonium hydroxide; and

(n) DEEA: 2-diethylaminoethanol.

Preparative Procedures CAPOs may be prepared by forming a starting reaction mixture by adding aluminum chlorhydrol or aluminum oxide to a solution of chromium acetate hydroxide in water, then adding successively phosphoric acid and the .templating agent. Between each addition, and after formation of the final mixture, the mixture is blended until a homogeneous mixture is observed.

Alternatively, the phosphoric acid may be mixed with at least part of the water, and aluminum oxide or isopropoxide mixed in. A solution of chromium acetate hydroxide is then added, followed by the templating agent, and the resultant mixture mixed until homogeneous. In a third procedure, amorphous chromium phosphate is ground dry with aluminum oxide and the resultant dry mixture added to an aqueous solution of phosphoric acid in an ice bath. The templating agent is then added, and the final mixture mixed until homogeneous.

Whichever technique is employed to produce the reaction mixture, this mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150 ^β C or 200 ^β C) for a time or placed in lined screw top bottles for

-133- digestion at 100°C. Digestions are typically carried out under autogenous pressure.

GaAPO MOLECULAR SIEVES

The GaAPO molecular sieves of U.S. Serial No. 599,771, filed April 13, 1984, and U.S. Serial No.

830,890 filed February 19, 1986 have a framework structure of GaO ~, A10 ~ and P0 ₂ tetrahedral units and have an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Ga _χ Al _y P _z )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(GaxAIyPJz O-2 and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "x", "y" and "z" represent the mole fractions of the elements gallium, aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point A B C D E F

In general, the value of "z" in the GaAPO molecular sieves is not greater than about 0.60.

In a preferred subclass of the GaAPO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

Mole Fraction Point _. x* y. z. a 0.01 0.59 0.40 b 0.01 0.34 0.65

C 0.34 0.01 0.65 d 0.59 0.01 0.40 In an especially preferred subclass of the

GaAPO molecular sieves the values of x, y and z are as follows:

Point e f g h i j

GaAPO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of gallium, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50 ° C and about 250*C, and preferably between about 100"C and about 200°C, until crystals of the GaAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 4 hours to about 20 days, and preferably about 1 to about 7 days, have

been observed. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the GaAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Ga _χ Al _y P _z )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 1.0; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably between about 2 and about 20; and "x", "y" and "z" represent the mole fractions of gallium, aluminum and phosphorus, respectively, ^• and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point G H I J K

Especially preferred reaction mixtures are those containing from 0.2 to 0.5 mole of Ga-0 and from 0.3 to 1 mole of Al --_,0O- for each mole of P Z„0 D_.

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "x", "y" and "z" such that (x 4- y 4- z) = 1.00 mole. Molecular sieves containing gallium, aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents GaAPO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare GaAPOs include:

(a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide;

(c) H_P0 ₄ : 85 weight percent aqueous phosphoric acid; (d) gallium sulfate or gallium(III) hydroxide;

(e) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(f) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (g) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH;

(h)- -c ₃ N: tri-n-propylamine, (C ₃ H._) ₃ N; (i) Quin: Quinuclidine, (C ₇ H_ ₃ N) ; (j) MQuin: Methyl Quinuclidine hydroxide, (C ₇ H ₁₃ NCH ₃ 0H) ; (k) C-hex: cyclohexylamine;

(1) TMAOH: tetramethy1 mmonium hydroxide; (m) TPAOH: tetrapropylammonium hydroxide; and (n) DEEA: 2-diethylaminoethanol. Preparative Procedures GaAPOs may be prepared by forming a starting reaction mixture by mixing the phosphoric acid with at least part of the water. To this solution the aluminum oxide or isopropoxide is added. This mixture is then blended until a homogeneous mixture is observed. To this mixture the gallium sulfate or gallium hydroxide and the templating agent are successively added and the resulting mixture blended until a homogeneous mixture is observed.

Alternatively, the aluminum oxide may be mixed with a solution of the gallium sulfate or hydroxide, and then the phosphoric acid and the templating agent

successively added. The resulting mixture is then blended until a homogeneous mixture is observed.

In a third process, the templating agent may be dissolved in water, the gallium hydroxide or sulfate added with stirring, a solution of the phosphoric acid added, and finally the aluminum oxide mixed in. The resulting mixture is then blended until a homogeneous mixture is observed.

Whichever technique is employed to form the reaction mixture, the mixture is then placed in a lined, (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150*C or 200*C) for a time or placed in lined screw top bottles for digestion at 100'C. Digestions are typically carried out under autogenous pressure.

GeAPO MOLECULAR SIEVES The GeAPO molecular sieves of U.S. Serial No. 599,807, filed April 13, 1984, and U.S." Serial No. 841,753 filed March 20, 1986 have a framework structure of Ge0 ₂ , A10 ~ and P0 ₂ tetrahedral units and have an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Ge _χ Al _y P ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" • represents the molar amount of "R" present per mole of

(Ge„xA1,yPJz 0.2 and has a value of zero to about 0.3, but is preferably not greater than 0.2; and "x", "y" and "z" represent the mole fractions of the elements germanium, aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole F act n Point A B C D E In a preferred subclass of the GeAPO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

Mole Fraction

X z 0.60 0.39

0.47 0.52

0.225 0.275

0.40 0.10 0.60 0.10

An especially preferred subclass of the GeAPO molecular sieves are those in which the value of "x" is not greater than about 0.13.

GeAPO compositions are generally synthesized by hydrothermal.crystallization from a reaction mixture containing reactive sources of germanium, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50 ^β C and about 250°C, and preferably between about 100°C and about 200*C, until crystals of the GeAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 2 hours to about 20 days, and preferably about 1 to about 10 days, have been observed. The product is recovered by any convenient method such as centrifugation or filtration. In synthesizing the GeAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Ge _χ Al _y P ₂ )0 ₂ : bH ₂ 0

wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.6; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably between about 10 and about 60; and "x", "y" and "z" represent the mole fractions of germanium, aluminum and phosphorus, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Fractio Point F G H I J

Especially preferred reaction mixtures are those containing from 0.2 to 0.4 mole of Ge0 ₂ and from 0.75 to 1.25 mole of 1 ₂ 0 ₃ for each mole of ₂ 0 ₅ -

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "x", "y" and "z" such that (x 4- y 4- z) = 1.00 mole. Molecular sieves containing germanium, aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents GeAPO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare GeAPOs include:

(a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide;

(c) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid; (d) germanium tetrachloride, germanium ethoxide and germanium dioxide;

(e) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(f) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(g) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH; (h) Pr ₃ N: tri-n-propylamine, (C ₃ H ₇ ) ₃ N; (i) Quin: Quinuclidine, (C ₇ H- ₃ N) ;

(j) MQuin: Methyl Quinuclidine hydroxide, (C _? H ₁₃ NCH ₃ OH) ;

(k) C-hex: cyclohexylamine;

(1) TMAOH: tetramethy1ammonium hydroxide; (m) TPAOH: tetrapropylammonium hydroxide; and (n) DEEA: 2-diethylaminoethanol. Preparative Procedures In some cases, it may be advantageous, when synthesizing the GeAPO compositions, to first combine sources of germanium and aluminum, to form a mixed germanium/aluminum compound (this compound being typically a mixed oxide) and thereafter to combine this mixed compound with a source of phosphorus to form the final GeAPO composition. Such mixed oxides may be prepared for example by hydrolyzing aqueous solutions containing germanium tetrachloride and aluminum chlorhydrol, or aluminum tri-sec-butoxide. GeAPOs may be prepared by forming a starting reaction mixture by mixing the phosphoric acid with at least part of the water. To this solution is added the mixed germanium/aluminum oxide prepared as described above. This mixture is then blended until a homogeneous mixture is observed. To this mixture the templating agent is added and the resulting mixture blended until a homogeneous mixture is observed.

Alternatively, to a solution of aluminum isopropoxide may be added germanium ethoxide. The resultant solution may optionally be dried to produce a mixed oxide. To the mixed solution or dried oxide are

added successively the phosphoric acid and the templating agent. The resulting mixture is then blended until a homogeneous mixture is observed.

In a third process, a solution is formed by dissolving the phosphoric acid in water, adding aluminum oxide or isopropoxide and mixing thoroughly. To the resultant mixture is added a solution containing the templating agent and germanium dioxide. The resulting mixture is then blended until a homogeneous mixture is observed.

Whichever technique is employed to form the reaction mixture, the mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150"C or 200 ^β C) for a time or placed in lined screw top bottles for digestion at 100*C. Digestions are typically carried out under autogenous pressure.

LiAPO MOLECULAR SIEVES The LiAPO molecular sieves of U.S. Serial No. 599,811, filed April 13, 1984, and U.S. Serial No. 834,921 filed February 28, 1986 have a framework structure of Li0 ₂ —3, A10 ₂ — and P0 ₂ 4* tetrahedral units and have an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (Li _χ Al _y P ₂ )0 ₂

wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(LixA1,yPz)02_ and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "x", "y" and "z" represent the mole fractions of the elements lithium, aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and ¹¹ z" are generally defined as being within the limiting compositional values or points as follows:

Mole F act o

In a preferred subclass of the LiAPO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

Point a b c d

In an .especially preferred subclass of the LiAPO molecular sieves the values of x, y and z are within the following limits: Mo e ract on

LiAPO compositions are generally synthesized by hydro-thermal crystallization from a reaction mixture containing reactive sources of lithium, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as

polytetrafluoroethylene and ^" heated ^" , preferably under autogenous pressure at a temperature between about 50°C and about 250 ^β C, and preferably between about 100 ^β C and about 200 ^β C until crystals of the LiAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 12 hours to about 5 days, have been observed. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the LiAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (Li _χ Al _y P ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; ."a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 2; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 40; and "x", "y" and "z" represent the mole fractions of lithium, aluminum and phosphorus, respectively, and each has a value of at least 0.01. In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z"

are generally defined as being within the limiting compositional values or poirits as follows i

Mole Fraction Point G H I J K In an especially preferred subclass of the reaction mixtures, the values of "x", "y" and "z" are within the limiting compositional values or points as follows:

Point 1 m n o q

In the foregoing expression of the reaction ^' composition, the reactants are normalized with respect to the total of ^» x", "y" and "z" such that (x 4- y 4- z) = 1.00 mole. Since the exact nature of the LiAPO molecular sieves is not clearly understood at present, although

^■ all are believed to contain Li0 ₂ tetrahedra in the three-dimensional microporous crystal framework structure, it is advantageous to characterize the LiAPO molecular sieves by means of their chemical composition. This is due to the low level of lithium present in certain of the LiAPO molecular sieves prepared to date which makes it difficult to ascertain the exact nature of the interaction between lithium, aluminum and phosphorus. As a result, although it is believed that *k*.° ₂ tetrahedra are substituted isomorphously for A10 ₂ or P0 ₂ tetrahedra, it is appropriate to characterize certain LiAPO compositions by reference to their chemical composition in terms of the mole ratios of oxides. Molecular sieves containing lithium, aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents LiAPO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare LiAPOs include:

(a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide;

(c) H ₃ PO :.85 weight percent aqueous phosphoric acid;

(d) lithium sulfate or lithium orthophosphate;

(e) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; (f) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (g) . Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH; (h) P* _* c ₃ * : tri-n-propylamine, (C ₃ H ₇ ) ₃ N; (i) Quin: Quinuclidine, (C ₇ H- ₃ N) ; (j) MQuin: Methyl Quinuclidine hydroxide,

(C _? H ₁₃ NCH ₃ 0H) ; (k) C-hex: cyclohexylamine; (1) TMAOH: tetramethylammonium hydroxide; (m) TPAOH: tetrapropylammonium hydroxide; and (n) DEEA: 2-diethylaminoethanol.

Preparative Procedures LiAPOs may be prepared by forming a starting reaction mixture by suspending aluminum oxide in at least part of the water. To this mixture the templating agent is added. The resultant mixture is then blended* until a homogeneous mixture is observed. To this mixture the lithium phosphate or sulfate is added and the resulting mixture blended until a homogeneous mixture is observed. Alternatively, an initial mixture may be formed by mixing aluminum oxide and lithium phosphate or sulfate. To the resultant mixture are

added successively phosphoric acid and an aqueous solution of the templating agent, and the resulting mixture blended until a homogeneous mixture is observed. In a third procedure, the phosphoric acid is mixed with at least part of the water, and the aluminum oxide is mixed in. To the resultant mixture are added lithium sulfate and the templating agent, and the resulting mixture blended until a homogeneous mixture is observed. Whichever procedure is adopted to form the reaction mixture, the mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150°C or 200 ^β C) for a time or placed in lined screw top bottles for digestion at 100 ^β C. Digestions are typically carried out under autogenous pressure.

FeTiAPO MOLECULAR SIEVES The FeTiAPO molecular sieves of U.S. Serial No. 599,824, filed April 13, 1984, and U.S. Serial No. 902,129 filed September 2, 1986 have three-dimensional microporous framework structures of Fe0 ₂ ⁿ , Ti0 ₂ , A10 ₂ ~ and P0 ⁺ tetrahedral oxide units having an empirical chemical composition on an anhydrous basis expressed by the.formula: mR : (M _χ AlyP _z )0 ₂

wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "M" represents iron and titanium; "m" represents the molar amount of "R" present per mole of (M _x Al _y P ₂ )0 ₂ and has a value of zero (0) to about 0.3; and "x", "y" and "z" _. represent the mole fractions of "M", aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions ^" "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole Fraction Point A B C D E

In a preferred subclass of the FeTiAPO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

FeTiAPO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of iron, titanium, aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50 ^β C and about 250*C, and preferably between about 100°c and about 200*C until crystals of the FeTiAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 12 hours to about 5 days, have been observed. The product is recovered by

- any convenient method such a≤ centrifugation or filtration.

In synthesizing the FeTiAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (M _χ Al _y P ₂ )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300; and "x", "y" and "z" represent the mole fractions of "M" (iron and titanium, aluminum and phosphorus, respectively, and each has a value of at least 0.01.

In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows: Mo Fraction

Point F G H I J

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "x", "y" and "z" such that (x 4- y 4- z) = 1.00 mole. ^• 5 Molecular sieves containing iron, titanium, aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents FeTiAPO compositions may be prepared by using 0 numerous reagents. The preferred sources of iron and titanium for preparing FeTiAPOs are the same as those for preparing the FeAPOs and TiAPOs already described above. Other reagents which may be employed to prepare FeTiAPOs include: 5 (a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide;

(c) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid;

(d) TEAOH: 40 weight percent aqueous solution 0 of tetraethylammonium hydroxide;

(e) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(f) Pr ₂ NH: di-n-propylamine, (C ₃ H _? ) ₂ NH;

(g) Pr ₃ N: tri-n-propylamine, (C ₃ H ₇ ) ₃ N; 5 (h) Quin: Quinuclidine, (C ₇ H ₁₃ N) ;

(i) MQuin: Methyl Quinuclidine hydroxide,

(C _? H ₁₃ NCH ₃ OH) ; (j) C-hex: cyclohexylamine; (k) TMAOH: tetramethylammonium hydroxide; (1) TPAOH: tetrapropylammonium hydroxide; and

(mj ^" DEEA: 2-diethylaminoethanol.

Preparative Procedures FeTiAPOs may be prepared by forming a homogeneous reaction mixture containing reactive sources of iron, titanium, aluminum and phosphorus. The reaction mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150 ^e C or 200"C) for a time or placed in lined screw top bottles for digestion at 100"C. Digestions are typically carried out under autogenous pressure.

XAPO MOLECULAR SIEVES The XAPO molecular sieves of* U.S. Serial No. 599,810, filed April 13, 1984, and U.S. Serial No. 902,020 filed September 2, 1986 have a three-dimensional microporous framework structures of M0 ₂ ⁿ , A10 ₂ ~ and Pθ ₂ ⁺ tetrahedral oxide units having an empirical chemical composition on an anhydrous basis expressed by the formula: mR : (M _x AlyP _z )0 ₂

wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "M" represents at least one element from each of the classes of: 1) iron and titanium; and 2) cobalt, magnesium, manganese and zinc; "n" is 0, -1 or -2; "m" represents a molar amount of "R" present per mole of (M _x AlyP _z )0 ₂ and has a value of zero (0) to about 0.3; and "x", "y" and "z" represent the mole fractions of "M", aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Mole F action Point A B C D E In a preferred subclass of the XAPO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

Point a b c d e f

XAPO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of "M", aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a sealed pressure vessel, preferably lined with an inert plastic material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50'C and about 250"C, and preferably between about 100'C and about 200*C until crystals of the XAPO product are obtained, usually a period of from several hours to several weeks. Typical effective times of from 2 hours to about 30 days, generally from about 2 hours to about 20 days, have been observed. The product is recovered

by any convenient method such as centrifugation or filtration.

In synthesizing the XAPO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : (M _χ Al _y P ₂ )0 ₂ : bH.,0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6; "M" represents at least one element from each of the classes of: 1) iron and titanium; and 2) cobalt, magnesium, manganese and zinc; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300; and "x", "y" and "z" represent the mole fractions of "M" (iron and/or titanium, and at least one of cobalt, magnesium, manganese and zinc) , aluminum and phosphorus, respectively, and each has a value of at least 0.01, with the proviso that "x" has a value of at least 0.02.

In one embodiment the reaction mixture is selected such that the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point F G H I J

In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of ^» x", "y" and "z" such that (x 4- y 4- z) = 1.00 mole.

XAPO molecular sieves are prepared as follows:

Preparative Reagents XAPO compositions may be prepared by using numerous reagents. The preferred sources of elements "M" for preparing XAPOs are the same as those for preparing other APOs containing the same elements, as described above and below. Other reagents which may be employed to prepare XAPOs include: (a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide;

(c) H ₃ PO : 85 weight percent aqueous phosphoric acid;

.(.d) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide;

(e) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide;

(f) Pr ₂ NH: di-n-propylamine, (C ₃ H _? ) ₂ NH;

(g) Pr ₃ N: .tri-n-propylamine, (C ₃ H _? ) ₃ N; (h) Quin: Quinuclidine, (C ₇ H_ ₃ N) ;

(i) MQuin: Methyl Quinuclidine hydroxide,

. (C _? H ₁₃ NCH ₃ OH) ; (j) C-hex: cyclohexylamine; (k) TMAOH: tetramethylammonium hydroxide; (1) TPAOH: tetrapropylammonium hydroxide; and

(m) DEEA: 2-diethylaminoethanol.

Preparative Procedures XAPOs may be prepared by forming a homogeneous reaction mixture containing reactive sources of elements "M", aluminum and phosphorus. The reaction mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150 ^β C or 200 ^* C) for a time or placed in lined screw top bottles for digestion at 100 ^β C. Digestions are typically carried out under autogenous pressure.

MIXED-ELEMENT APO MOLECULAR SIEVES The mixed element APO molecular sieves of U.S. Serial No. 599,978, filed April 13, 1984, and U.S. Serial No. 846,088 filed March 31, 1986 have a framework structure of M0 ₂ , A10 ₂ and P0 ₂ tetrahedral units,

wherein M0 ₂ represents at least two different ^" elements present as tetrahedral units "M0 ₂ ⁿ " with charge "n", where "n" may be -3, -2, -1, 0 or +1. One of the elements "M" is selected from the group consisting of arsenic, beryllium, boron, chromium, gallium, germanium, lithium and vanadium, while a second one of the elements "M" is selected from the group consisting of cobalt, iron, magnesium, manganese, titanium and zinc. Preferably, "M" is a mixture of lithium and magnesium. The mixed-element molecular sieves have an empirical chemical composition on an anhydrous basis expressed by the formula: mR :. (M _χ Al _y P ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(LixAl.yPz)02, and has a value of zero to about 0.3, but is preferably not greater than 0.15; and "x", "y" and "z" represent the mole fractions of the elements "M" (i.e. "x" is the total of the mole fractions of the two or more elements "M") , aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

Point A B C

D E

In a preferred subclass of the mixed-element APO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

Mole Fraction Point a b c d e f

An especially preferred subclass of the mixed- element APO molecular sieves are those in which the value of x is not greater than about 0.10.

A second group (FCAPO's) of mixed element APO molecular sieves described in U.S. Serial No. 600,171, filed April 13, 1984 (now U. S. Patent No. 4,686,093 issued August 11, 1987) , have a framework structure of M0 ₂ ⁿ , AIO ~ and P0 ₂ ⁺ tetrahedral units, wherein M0 ₂ ⁿ

represents at least two different elements which are present as tetrahedral units. " 0 ₂ ⁿ " with charge "n", where "n" may be -3, -2, -1, 0 or 4-1 and which are selected from the group consisting of arsenic, beryllium, boron, chromium, gallium, germanium, lithium and vanadium. ^' These mixed-element molecular sieves have an empirical chemical composition on an anhydrous basis expressed by the formula:

* ^: < ^H x ^A1 y ^P z>°2 wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the molar amount of "R" present per mole of

(MxAly.PzJ02_ and has a value of zero to about 0.3; and

"x", "y" and "z" represent the mole fractions of the elements "M" (i.e. "x" is the total of the mole fractions of the two or more elements "M") , aluminum and phosphorus, respectively, present as tetrahedral oxides. The mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows:

In a preferred subclass of these mixed-element APO molecular sieves the values of x, y and z are within the limiting compositional values or points as follows:

Mole Fract o

The mixed-element APO compositions are generally synthesized by hydrothermal crystallization from a reaction mixture containing reactive sources of the elements "M", aluminum and phosphorus, preferably an organic templating, i.e., structure-directing, agent, preferably a compound of an element of Group VA of the Periodic Table, and/or optionally an alkali or other metal. The reaction mixture is generally placed in a

sealed pressure vessel, preferably lined with an inert plastic-material such as polytetrafluoroethylene and heated, preferably under autogenous pressure at a temperature between about 50"C and about 250*C, and preferably between about 100 ^* C and about 200*C until crystals of the APO product are obtained, usually a period of from several hours to several weeks. Typical effective times of ^' from 2 hours to about 30 days, generally from about 2 hours to about 20 days, and preferably about 12 hours to about 5 days, have been observed. The product is recovered by any convenient method such as centrifugation or filtration.

In synthesizing the mixed-element APO compositions, it is preferred to employ a reaction mixture composition expressed in terms of the molar ratios as follows: aR : CM _χ Al _y P ₂ )0 ₂ : bH ₂ 0 wherein "R" is an organic templating agent; "a" is the amount of organic templating agent "R" and has a value of from zero to about 6 and is preferably an effective amount within the range of greater than zero (0) to about 6, and most preferably not more than about 0.5; "b" has a value of from zero (0) to about 500, preferably between about 2 and about 300, most preferably not greater than about 20, and most desirably not more than about 10; and "x", "y" and "z" represent

the mole fractions of "M", aluminum and phosphorus, respectively, "y" and "z" each having a value of at least 0.01 and "x" having a value of at least 0.02, with each element "M" having a mole fraction of at least 0.01.

In one embodiment the reaction mixture is selected such- that the mole fractions "x", "y" and "z" are generally defined as being within the limiting compositional values or points as follows: Mole Fraction

Point F G H I J

Preferred reaction mixtures are those containing not more than about 0.2 moles of the metals "M" per mole of phosphorus. In the foregoing expression of the reaction composition, the reactants are normalized with respect to the total of "x", »y" and "z» such that (x 4- y 4- z) = 1.00 mole.

Since the exact nature of the mixed-element APO molecular sieves is not clearly understood at present, although all are believed to contain M0 ₂

tetrahedra in the three-dimensional microporous crystal framework structure, it is advantageous to characterize the mixed-element APO molecular sieves by means of their chemical composition. This is due to the low level of the elements "M" present in certain of the mixed-element APO molecular sieves prepared to date which makes it difficult to ascertain the exact nature of the interaction between the metals ^W M", aluminum and phosphorus. As a result, although it is believed that 0 ₂ tetrahedra are substituted isomorphously for A10 ₂ or P0 ₂ tetrahedra, it is appropriate to characterize certain mixed-element APO compositions by reference to their chemical composition in terms of the mole ratios of oxides. Molecular sieves containing the metals "M", aluminum and phosphorus as framework tetrahedral oxide units are prepared as follows:

Preparative Reagents Mixed-element APO compositions may be prepared by using numerous reagents. Reagents which may be employed to prepare mixed-element APOs include:

(a) aluminum isopropoxide;

(b) pseudoboehmite or other aluminum oxide;

(c) H ₃ P0 ₄ : 85 weight percent aqueous phosphoric acid;

(d) lithium phosphate or magnesium hydroxide

or appropriate salts of the other elements "M", as described above;

(e) TEAOH: 40 weight percent aqueous solution of tetraethylammonium hydroxide; (f) TBAOH: 40 weight percent aqueous solution of tetrabutylammonium hydroxide; (g) Pr ₂ NH: di-n-propylamine, (C ₃ H ₇ ) ₂ NH; (h) Pr ₃ N: tri-n-propylamine, (C ₃ H _? ) ₃ N; (i) Quin: Quinuclidine, (C.-H--N) ; (j) MQuin: Methyl Quinuclidine hydroxide,

(C ₇ H ₁₃ NCH ₃ OH) ; (k) C-hex: cyclohexylamine; (1) TMAOH: tetramethylammonium hydroxide; ( ) TPAOH: tetrapropylammonium hydroxide; and (n) DEEA: 2-diethylaminoethanol.

Preparative Procedures Mixed element APOs may be prepared by forming a starting reaction mixture by mixing aluminum oxide, magnesium hydroxide, lithium phosphate (or the corresponding salts of the other elements "M") . To this mixture the phosphoric acid is added. The resultant mixture is then blended until a homogeneous mixture is observed. To this mixture the templating agent is added and the resulting mixture blended until a homogeneous mixture is observed.

The reaction mixture is then placed in a lined (polytetrafluoroethylene) stainless steel pressure vessel and digested at a temperature (150 ^β C or 200 ^β C) for a time or placed in lined screw top bottles for digestion at 100*C. Digestions are typically carried out under autogenous pressure.

SILICOALUMINOPHOSPATE MOLECULAR SIEVES The preferred NZMSs, to date, are the silicoaluminophosphate molecular sieves described in U.S. Patent No. 4,440,871, and U.S. Serial No. 575,745, filed January 31, 1984. The use of such catalysts in reforming catalysts or as components in heretofore employed refor ing/dehydrocyclization catalysts provides improved catalysts and provides products characterized by an improved selectivity to iso-products and provides improved activity in reforming/dehydrocyclization reactions.

The silicoaluminophosphate molecular sieves of U.S. Patent No. 4,440,871 and the aforementioned application Serial No. 575,745, are disclosed as microporous crystalline silicoaluminophosphates, the pores of which are uniform and have nominal diameters of greater than about 3 Angstroms and whose essential empirical chemical composition in the as-synthesized and anhydrous form is:

^* ** : (Si _χ Al _y P-)0-

wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the moles of "R" present per mole of (Si Al PJO, and has a value of from 0.02 to 0.3; "x", "y" and "z" represent the mole fractions of silicon, aluminum and phosphorus, respectively, present as tetrahedral oxides, said mole fractions being such that they are within the pentagonal compositional area defined by points A, B, C, D and E of the ternary diagram of FIG. 5 of the aforementioned U.S. Patent No. 4,440,871, and are preferably within the pentagonal compositional area defined by points a, b, σ, d and e of FIG. 6 of this patent. The SAPO molecular sieves of U.S. Patent No. 4,440,871 and the aforementioned application Serial No. 575,745 are also described as silicoaluminophosphates having a three-dimensional microporous framework structure of P0 ₂ , AIO ~ and Si0 ₂ tetrahedral units, and whose essential empirical chemical composition on an anhydrous basis is: mR : (Si _χ Al _y P ₂ )0 ₂ wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" represents the moles of "R" present per mole of (Si Al PJO, and has a value of from zero to 0.3; "x", "y" and "z" represent, respectively, the mole fractions of silicon, aluminum and phosphorus present in the oxide

^• moiety, said mole fractions being within the compositional area bounded by points A _/ B, C, D and E on the ternary diagram which is FIG. 5 of the aforementioned patent, said silicoaluminophosphate having a characteristic X-ray powder diffraction pattern which contains at least the d-spacings set forth below in any one of-Tables I, III, V, VII, IX, XIII, XVII, XXI, XXIII or XXV of U.S. Patent No. 4,440,871. Further, the as-synthesized crystalline silicoaluminophosphates of U.S. Patent No. 4,440,871 may be calcined at a temperature sufficiently high to remove at least some of any organic templating agent present in the intracrystalline pore system as a result of such synthesis. The silicoaluminophosphates of U.S. Patent No. 4,440,871 are generally referred to therein as

"SAPO", as a class, or as "SAPO-n" wherein "n" is an integer denoting a particular SAPO as its preparation is reported in U.S. Patent No. 4,440,871. The preparation of the SAPOs is disclosed in U.S. Patent No. 4,440,871, incorporated herein by reference.