BACKGROUND OF THE INVENTION

The field of the invention is increasing the capacity of landfills. The prior art on the processing of solid waste is voluminous.

SUMMARY OF THE INVENTION

The present invention is a method of landfill mining which comprises converting an existing landfill to an aerobic processor, and then excavating the landfill to remove decomposed waste which may be sold or used for a number of purposes. The efficiency of the aerobic processor is related to its content and temperature. The temperature of such a landfill aerobic processor may be controlled by controlling the rate and location of the injection of air, water and a raw material (such as sewage sludge), and the venting of depleted air and moisture. The water that is injected may comprise Ieachate, which is the aqueous liquid that may be drained from the bottom of the landfill and recycled.

The present invention also includes a method of controlling the temperature in a landfill that comprises selectively injecting air, water and possibly a raw material (such as sewage sludge), and selectively venting depieted air and moisture. The seiection includes rate and location. The water that is injected may comprise Ieachate, which is the aqueous liquid that may be drained from the bottom of the landfill and recycled.

The present invention increases the capacity of a landfill. The volume of the landfill that was previously occupied by the decomposed waste, is now available for re-use and may be filled by additional sold waste, in a preferred embodiment of the invention, the method of landfill mining comprises the following steps: (1 ) converting the landfill to aerobic production by injection of moisture and air, and a raw material such as sewage sludge (if required), thereby increasing the rate of waste decomposition; (2) excavating the landfill to remove material; (3) separating the removed material to substantially isolate at least one segregated material from the residual material; (4) disposing of at least one segregated material; and (5) returning the residual material to the landfill. The segregated material preferably includes decomposed waste and recyclables, and may also include toxic material and hazardous waste.

BRIEF DESCRIPTION OF THE DRAWING

Figure 1 is schematic section view of a landfill.

DETAILED DESCRIPTION OF THE INVENTION

Solid waste is produced at a steadily increasing rate around the world. There are numerous methods for dealing with the disposal of solid waste. One of the primary methods is the landfill. Generally speaking, the use of a landfill to dispose of solid waste includes the following steps: location of the site of the landfill; purchase or lease of the land; excavation of the land to produce suitable receiving cells; placing solid waste on the prepared cells; and after the cells have been filled to the maximum height, covering the cells and closing the landfill. A number of these steps are quite complex. For example, selecting the correct site involves consideration of the soils both on the surface and in the location of the proposed cells, evaluation of ground water patterns around the proposed site, and reviewing input from those who would be affected by a landfill at the proposed site. The excavation of the cells may include the

additional step of lining the cells with a particular type of soil and plastic liner, before depositing solid waste in the cell.

Before the present invention, one of the primary problems with landfills was the fact that the capacity (called "air space") would become exhausted. This would create the need to open a new landfill, as well as maintain the existing landfill during closure. The present invention may reduce or eliminate these problems by increasing the capacity of existing landfills.

In one form, the present invention comprises the step of converting an existing landfill to an aerobic processor, and then selectively excavating the landfill to remove decomposed waste, thereby increasing the capacity of the landfill. In the preferred embodiments, there are additional steps to improve the efficacy of the invention.

In a preferred embodiment, the landfill is converted to aerobic production.

Most landfills are designed to be anaerobic, in which the landfill is designed to be dry tomb, devoid of air and moisture. The conversion of such a conventional landfill from anaerobic to aerobic production, requires the injection of air and moisture into the landfill, in order to maximize the rate of waste decomposition.

The aerobic production converts most of the waste in the landfill, which is comprised mainly of organic materials, into a useful product. The resulting processed soil/compost may then be excavated and used for a number of purposes. For example, the excavated, processed soil/compost may be sold as a soil amendment, or may be used as landfill cover.

The injection of moisture and air into a landfill substantially increases the rate of decomposition of the organic materials. The reaction rate may be increased by a factor of ten (10) or more by injection of appropriate amounts of air and moisture, depending on the composition of the material in the cell of the landfill, the age of the landfill, the conditions under which the landfill was maintained in the past, and other factors. The injection of moisture into the

landfill is preferably carried out to achieve from about 50% to about 70% water and from about 30% to about 50% solids by weight in the cell. More preferably, the injection of moisture into the landfill is carried out to achieve about 60% water and about 40% solids by weight in the cell. The injection of air into the landfill is preferably carried out to achieve a temperature of from about 140° to about 1 80°F (about 60° to about 82°C) in the cell of the landfill. More preferably, the injection of air into the landfill is carried out to achieve a temperature of about 170°F (about 77°C) in the cell of the landfill.

Since the landfill is large and self insulating, a cooling mechanism must be included to carry off the heat of the aerobic composting reaction. This is done by injecting the water first to achieve from about 50% to about 70% and preferably about 60% (by weight) level. Then the air injection can commence always making sure that the exhaust gases are from about 5% to about 1 5%, and preferably about 10% oxygen (dry basis) or twice the stoichiometric requirement of the composting reaction. The heat of reaction will turn the injected water into water vapor that will be carried off by the fixed gases, nitrogen, oxygen and carbon dioxide. If the temperature increases above from about 140° to about 1 80°F (about 60° to about 82°C), and preferably about 1 70°F (about 77°C), then additional air and water as needed may be injected. If the temperature falls below about 1 70°F (about 77°C), then raw materials such as fertilizing materials and sewage sludge can be added to the injection. This increases nitrogen to carbon ratio and thereby the rate of biological composting reaction. The aerobic reaction can be further stabilized by the reinjection of the Ieachate drained from the landfill along with the make-up water as required.

The specific design of the apparatus for the injection of air and water into the landfill to promote the aerobic composting reaction will vary with the specific requirements of the landfill to be treated. The general design of a preferred embodiment as shown in Figure 1 includes the venting 1 of depleted

air and water vapor at the top of the landfill and the venting 2 of depleted air, water vapor and Ieachate at the bottom. Each is accomplished with a series of perforated pipes in roughly planar form conforming to the top 3 and bottom 4 of the landfill. The pipes are spaced about 10 feet (about 3 meters) apart depending on the density of the waste to be processed. Between these two vent planes are placed alternating injection 5 and vent 6 planes of pipes at about ten foot (about three meters) horizontal and/or diagonal spacing. The perforated injection pipes carry air, make-up water, and Ieachate with sludge injection 7 as needed to maintain the desired reaction rate. The piping system may be valved 8 so that different parts of the cell can be treated with greater or lesser flows in order to accommodate variations in refuse properties especially in large thick cells. The flow programming of the injection into the landfill is preferably based on the measurement of temperature in the cell, and on the oxygen/carbon dioxide content of the off gas from the cell. The measurement of temperature is preferably taken at a plurality of locations in the cell. Depending on the nature of the landfill and the cell, an instrumentation pipe with a plurality of temperature and/or oxygen (0 ₂ ) sensors, such as one sensor placed about every two feet (about 0.6 meter) along the length of the pipe may be inserted into an injection or vent pipe to determine the temperature profile in the refuse mass adjacent to the installed pipe as required. A log of the temperature readings at each location and the oxygen/carbon dioxide content of the off gas at each location is preferably kept so as to monitor the refuse mass in the cell of the landfill. There must be careful monitoring to insure that an adequate rate of decomposition is achieved throughout the cell, while avoiding the ignition temperature of the refuse mass. Depending on the circumstances, the temperature of the refuse mass may be reduced by injecting additional air at a higher rate, and additional moisture at a higher rate, so as to cool the refuse mass. The constant monitoring of the temperature of the refuse mass and the oxygen/carbon dioxide content of the off gas is required in part because the composition and density of the refuse mass is usually not known with sufficient certainty and specificity, so as to allow advance planning of the

precise rate of injection and the precise places of injection of air and moisture into the cell of the landfill.

The excavation of the landfill is preferably followed by a separation of the excavated materials. The separation will preferably separate the processed soil/compost from recyclable materials, and from any toxic materials and hazardous waste, thereby leaving the residual material. The recyclable materials such as glass, aluminum cans, iron materials and certain plastics, may then be recycled. Any hazardous waste and toxic materials found during the excavation may be processed (including bioprocessed) to contain or dispose of them in accord with known methods, and in accord with government regulations. The residual materials may be returned to the landfill.

In the present invention, the step of separating the material that is removed from the cell of the landfill, is carried out to substantially isolate at least one segregated material from the residual material. The primary segregated material is decomposed waste. Other segregated materials depend on the nature of the landfill and may include recyclabies, toxic materials, hazardous waste and other items. The segregated material is regarded as substantially isolated when the separation has been carried out to an extent that allows the segregated material to be used for its intended purpose or further processed. For example, if under the circumstances iron materials must be separated from aluminum cans in order to be suitable for recycling, then the separation must be carried out to this extent.

Some landfills were built using former technologies that have been replaced by better technologies. For example, a number of older landfills were not lined before the solid waste was placed into the cells. One embodiment of the invention for such landfills includes aerobic processing, excavating the landfill, removing all material in the landfill, and then lining the iandfill cells. Subsequently, the residual materials may be returned to the cells. The new capacity of the Iandfill may then be filled with new solid waste.

The present invention may allow the revitalization of some existing landfills that have been closed because the capacity was exhausted. This may result in additional environmental benefits. For example, if the closed Iandfill is located closer to the source of the solid waste, as compared to the currently operating Iandfill, then the revitalization of the formerly closed Iandfill under the method of the present invention could result in transportation of the solid waste over a shorter distance. This could result in less air pollution from trucks and other vehicles used to transport the solid waste.

Additional advantages of the invention include the elimination of methane and other noxious gases from the gases produced by the decomposition of the organic materials. This greatly reduces the risk of fire and explosion at the Iandfill and in adjacent communities. Another advantage resulting from the shift from anaerobic to aerobic decomposition in the Iandfill is the elimination of offensive odors, both during the decomposition and in the subsequent mining operation.

The process of the present invention may be carried out in single applications, or continuously. A single application of the process may be more suitable for a small Iandfill. The process of the invention could be carried in a small Iandfill, thereby increasing the capacity, which could be used for disposal of additional solid waste. For a larger landfill, the active area may be divided into a number of cells to be processed sequentially and continuously. For example, the first cell may be in aerobic production by the injection of moisture and air. The second cell may be in the process of excavation to remove materials. The third cell may be in the process of lining the cell to comply with current standards and technology. The fourth cell may be in the process of being filled by additional solid waste.

Variations of the invention may be envisioned by those skilled in the art and the invention is to be limited solely by the claims appended hereto.