Furthermore, the vast majority of incinerated organic material is converted into undesirable carbon dioxide and nitrous oxides, which are implicated in global warming, ozone layer depletion, and the formation of volatile organic compounds which contribute to smog problems in urban areas. The pyrolisis procedure involves the conversion of various materials into a Carbon-rich residue in an oxygen depleted, high temperature environment. However, the high temperature, depleted oxygen environment of pyrolisis creates some extremely toxic compounds. Furthermore, pyrolisis is an inefficient method for disposing large volumes of waste materials due to the requirement that pyrolisis feed stocks must be pre-sorted and processed.

[0002] Many of the disadvantages of incineration and pyrolisis are overcome by waste gasification. Waste gasification involves supplying the minimum amount of oxygen necessary to cause a thermo-chemical reaction that releases combustible gases at a controlled temperature, without supplying enough oxygen to cause combustion. When feed stock waste materials that are rich in energy, as measured by British thermal units, are loaded into gasification reactor chambers, and are exposed to a controlled temperature, oxygen depleted environment, such solid, sludge, or liquid feed stock materials are converted into a produced fuel gas.

Materials that are rich in energy include, but are not limited to, coal, wood, cardboard, paper, industrial scrap, plastics, tires, organic wastes, sewage cake, animal waste, and crop residue, or combinations thereof. The released produced fuel gas is then mixed with oxygen and combusted as an alternative to the use of natural gas, diesel fuel, or propane. Examples of prior gasification systems are

shown in U. S. Pat. Nos. 4,941, 415 and 5,941, 184, the disclosures of which are incorporated by reference herein.

[0003] The material remaining after the completion of the gasification process cycle is composed of incombustible materials, including metals, glass, and ceramics, along with a fine inert salt and mineral power residue of low carbon content, and has a greatly reduced volume that is suitable for remanufacturing into concrete material or land filling. Furthermore, recyclable materials that do not undergo phase transition, such as all glass, aluminum, metals, and other non- combustible residuals, are recoverable after the gasification process, thereby eliminating the need for pre-sorting or processing the in-bound feed stock material.

[0004] Conventional prior art-gasification systems are multi-step processes that generally utilize four open-looped process steps. These four steps typically involve: one or more primary gasifiers; a central air mixing chamber; a secondary processor for combusting the produced fuel gas; and final air cleaning systems.

However, conventional gasification systems have proved to be somewhat difficult to cost-effectively construct. Therefore, a need exists for a simplified gasification apparatus that is inexpensive to build, simple to operate, and yet achieves the benefits of producing a gas fuel from solid waste feed stock materials.

[0005] Furthermore, prior art gasification systems have been designed for permanent installment at a particular location. These systems have high capital costs. The permanency of such systems prohibits the ability to move the waste disposal systems to a areas of need as job demands change or vary over time.

Therefore, there exists a need to provide a simplified gasification system that is both mobile and cost efficient in the disposal of waste materials while at the same time being able to meet the air emission standards set by federal and state environmental protection agencies. A low cost, small scale system that efficiently disposes of waste meets the needs of smaller waste generators and allows for waste disposal at the same location where it is generated, avoiding expensive cartage, sorting, and"tip"sees.

[0006] Current research indicates that increasing the surface area of the feed stock material that is exposed to gasification process gas significantly improves the

production rate of produced fuel gas from waste materials which translates into faster batch cycle times, further reducing operating costs. Yet, some prior art gasification systems, such as those illustrated in U. S. Pat. Nos. 6,439, 135 and 5,619, 938, utilize gasification reactor chamber configurations that expose only limited waste material surface area to gasification process gas. Such prior art systems typically incorporate gasification reactor chamber configurations where only the bottom of the feed stock at grate level, known as the primary reaction zone, and the uppermost surface of the feed stock, known as the secondary reaction zone, are exposed to optimum gasification conditions.

[0007] As a result, gasification of waste material that is not located at either the primary or secondary zones, such as that on the sides and center of the gasification chamber, requires that the temperature and/or duration of the gasification cycle be increased. Yet, higher gasification temperatures tend to reduce the Btu content of the resulting produced fuel gas. High operating temperatures also increase the time required for cooling the gasification reactor chamber to a temperature suitable for the loading and disposal of subsequent loads of waste materials. Longer cycle durations also greatly reduce the overall capacity of the system.

[0008] Furthermore, the costs associated with obtaining and maintaining higher gasification temperatures, along with the cost of fabricating a complex gasification reactor chamber that can withstand prolonged exposure to high temperatures, also increase. Some prior art gasification reactor chambers are lined with various clay- based insulative/refractory materials. These refractory materials maintain gasification reactor temperatures while also preventing structural damage to the gasification reactor chamber's steel superstructure and surface paint associated with prolonged exposure to excessive heat. Refractory material is usually applied to the gasification reactor chamber as pre-cast panels, bricks, or sprayed on as a gunnite-like application. Such refractory material is affixed to the exterior steel jacket of the gasification reactor chamber by refractory hangers, which are heavy metal dowels in the form of hooks. With typical prior art systems, a two to four inch layer of ceramic fiber blanket is usually inserted between the refractory material and the steel jacket before the refractory layer is installed to offer

additional thermal protection for the exterior steel surfaces of the gasification reactor chamber.

[0009] Application of refractory material is thus labor intensive, time consuming, and a significantly expensive step. Additionally, the weight of the refractory liner necessitates a expensive, high strength gasification chamber construction, such as a steel vessel constructed from at least 1/4 inch thick hot rolled A36 steel plate and heavy structurals. This additional weight of the superstructure further increases the overall cost of manufacturing, shipping, and installation.

[0010] An additional problem with the use of refractory material is the length of time required for cooling the gasification reactor chamber before it can be re-used to gasify a subsequent load of solid waste material. More specifically, a subsequent gasification process typically cannot begin until the gasification reactor chamber has cooled to approximately 150 degrees Fahrenheit. Yet, at the end of a process cycle, the clay refractory material tends to retain heat for a long period of time. Depending on the particular chemistry of the refractory material, this retention of heat may require that the gasification reactor chamber be inoperative for several hours as the temperature of the chamber, and associated refractory material, cools down.

[0011] The limited waste load capacity of prior art gasification systems often required the construction of multiple gasification reactor chambers to meet demand requirements. In previous designs, gasification reactor chambers typically have a rectangular configuration. As the length of the rectangular sidewalls is increased to satisfy larger feed stock capacity requirements, the size of the gasification reactor chamber creates problems associated with load density in various feed stocks in the gasification reactor chamber. This problem typically limits gasification reactor chambers to configurations that are approximately 20 feet high, 20 feet wide, and 20 feet long, accommodating approximately 50 tons of municipal solid waste. Larger configurations develop problems with the side load waste dump arrangement. More specifically, as the gasification chamber width extends beyond 20 feet, the angle of repose of the trash spilling out of the garbage truck and into the gasification chamber typically only fills a small portion of the

gasification reactor chamber's near sidewall, necessitating the addition of another load door in the roof of the gasification chamber.

[0012] Because the resulting produced fuel gas from the gasification of waste material has been produced in an environment that typically contains no more than 8% oxygen, waste gasification systems must also increase the level of ambient oxygen in the gas produced in the gasification reactor chamber to make it fully flammable. This often requires increasing the oxygen content of the produced fuel gas to approximately 15% to 20%.

[0013] Prior art gasification systems have typically increased the oxygen content of the produced fuel gas by directing the produced fuel gas through air mixing chambers. These mixing chambers are typically large, cylindrical vessels, with a variety of air induction tubes attached to multiple blower fans that flood the air mixing chambers with outside ambient air using air compressors or high velocity fans. Because of the large size of these chambers, they require substantial fabrication and installation time, and as a result are expensive. The use of fans and/or air compressors also increases the initial cost of the system and operating and maintenance expenses.

[0014] Conventional gasification systems also use cumbersome techniques for moving the produced fuel gas to the point of combustion. Such systems often vent, or breech, the fuel gas from the top or at least one side of the gasification reactor chamber, and direct the vented fuel gas from the gasification reactor chamber into a secondary gas processor, which is usually driven by a natural draft current that is created by hot air in the system rising through an exhaust stack. The fuel gas'exit from the gasification reactor chamber is controlled by a motor driven damper assembly that regulates the varying flow of produced fuel gas from this first process step into ducting that connects the gasification reactor chamber to the secondary air mixing chamber. Such systems typically require large diameter piping to draw the gas off from the gasification reactor chamber. This large piping, and associated ductwork, increases not only equipment cost, but also installation expenses.

[0015] A further disadvantage of traditional air draft systems is that produced fuel gases have a tendency to linger in the gasification reactor chamber, and become subject to accidental combustion, which ultimately lowers the Btu content of the extracted produced fuel gas. This problem is exacerbated by the inconsistency of up-draft air movement in a natural draft system. Humidity, wind, barometric pressure and outside temperature all affect the rate of flow through a natural draft system. This inconsistent flow causes the evacuation of gases from the gasification reactor chambers to frequently stall, produces negative results in the process, and adversely effects the total cycle time for the gasification of the feed stock material.

[0016] Additionally, the ability to withdraw and vent gases produced during the gasification process out from the gasification chamber affects the overall gasification process cycle time. More specifically, if the venting of produced gases from the gasification chamber is slower than the production rate of the gas, then the gasification chamber becomes back pressured, and the subsequent rate of gasification of the waste load becomes suppressed. For instance, it has been determined that the gasification of roughly 2 tons of solid waste material over a ten to twelve hour period can produce approximately 140 cfm of produced fuel gas.

However, because some prior art designs are only capable of moving approximately 9 to 15 cfm, the complete gasification of 2 tons of waste material could require more than 48 hours.

[0017] In instances in which oxygen levels have dipped below desired levels, prior art systems have introduced additional ambient air into the gasification chamber in order to raise oxygen levels. Yet, ambient air is comprised of approximately 78% nitrogen and 21% oxygen. Therefore, the use of ambient air as a process gas to obtain desired oxygen levels in the gasification chamber, results in the unavoidable inclusion of a large volume of nitrogen. Unfortunately, this additional volume of nitrogen to the gasification process contributes substantially to the formation and ultimate system air emission of nitrous oxides, which is an air emission contaminant that is currently regulated by the Environmental Protection Agency.

Replacing ambient air as a process gas with a high oxygen content gas, such as, but not limited to raw oxygen, would virtually eliminate the presence of nitrous oxides

in the produced exhaust stream as long as the combustion temperature the produced fuel gas is maintained below 2,100 degrees F.

[0018] Furthermore, in order to improve the combustibility of produced fuel gases that are produced by the gasification process, prior art systems have mixed produced fuel gases with ambient air. Such mixing has usually required that four parts of ambient air be mixed with one part of the produced fuel gas to sufficiently bring the produced fuel gas from its starved oxygen state (+/-9%) to one of maximum combustibility (17-20 %) Yet, as previously mentioned, thermal processes, such as flaring the mixture of produced fuel gas with ambient air, may result in the presence of regulated nitrous oxides in the gas exhaust stream.

Therefore, it is desirable to create a gasification system that may combust produced fuel gases without the formation of nitrous oxides.

[0019] Gasification system components that transport or contain this additional volume of ambient air must also be oversized to handle the accompanying large volumes of nitrogen. The presence of large volumes of nitrogen in ambient air also increases the size, associated fabrication costs, and weight of gasification systems.

For instance, the replacement of ambient air with raw oxygen could result in up to a 78% decrease in the amount of process gas that is required to enter into the gasification system. This signification reduction in volume may allow for a reduction in the size of the gasification chamber, which thereby would allow for a savings in material and fabrication costs and overall weight. Therefore, it would be desirable to have gasification system that may be constructed from smaller system components while still being capable of gasifying large quantities of waste materials.

[0020] It is therefore an object of the present invention to provide a gasification unit capable of gasifying waste materials at a reduced temperature and time.

[0021] It is a further object of the present invention to provide a gasification system that produces a high Btu content produced fuel gas from the gasification of a wide variety of un-processed and unsorted waste materials.

[0022] It is another object of the present invention to provide an inexpensive to build, simple to operate, mobile gasification unit that provides the benefits of producing a non-fossil fuel gas from these waste materials.

[0023] It is another object of the present invention to provide a mobile gasification unit in which a gasification control room and produced fuel gas combustion chamber may both be substantially located in a self contained unit.

[0024] It is a further object of the present invention to provide a mobile gasification unit that contains at least one gasification chamber equipped with a mesh liner for the purpose of substantially increasing the surface area of the primary thermo-chemical reaction zone, resulting in reduced system cycle times and a higher volume fuel gas production per unit of time.

[0025] It is a further object of the present invention to provide an improved gasification apparatus that is capable of venting produced fuel gases out of the primary gasification chamber at a sufficient rate so as to prevent the development of back pressure in that primary gasification chamber.

[0026] It is another object of the present invention to create a gasification system that may combust produced fuel gases with minimal formation of nitrous oxides.

[0027] It is a further object of the present invention to provide a gasification system that may be constructed from smaller system components while still being capable of gasifying similar or larger quantities of waste materials.

[0028] These and other desirable characteristics of the present invention will become apparent in view of the present specification, including the claims and drawings.

BRIEF SUMMARY OF THE INVENTION [0029] The present invention is directed to an apparatus that converts combustible solids, sludges, and liquids into a usable non-fossil fuel gas. More particularly, the present invention relates to a self-contained mobile gasification unit that includes at least one gasification chamber and a produced fuel gas combustion chamber.

Additionally, the present invention may be adapted to also include a control room, wherein the gasification chamber, produced fuel gas combustion chamber, and a

control room are all substantially located within the same self contained mobile gasification unit. The mobile gasification unit is preferably a container that has a standard configuration, such as that of a standardized sea cargo shipping container, so that the container may be easily transported from one location to another via a variety of intermodal modes of transportation, including, but not limited to, truck, train, or container ship.

[0030] A portion of the container is enclosed so as to form the at least one gasification chamber within the interior of the container. The size and number of gasification chambers within the container is dictated by the total waste processing volume desired and the overall size and configuration of the container. Each of the at least one gasification chambers are preferably comprised of an exterior vessel and an inner portion.

[0031] The exterior vessel is preferably, in part, comprised of at least a portion of the walls, base, and top portion of the container. Alternatively, the exterior vessel is comprised of walls within the container that are dedicated for the at least one gasification chamber. Additionally, the exterior vessel preferably includes a side partitioning wall that is positioned within the container. The partitioning wall preferably provides a common wall for the at least one gasification chamber and a produced fuel gas combustion chamber. Alternatively, the partitioning wall divides the portion of the container that is used for the gasification chamber from that which may be used for other aspects of the mobile gasification unit, such as both a control room and a produced fuel gas combustion chamber.

[0032] The exterior vessel also preferably includes doors, access ports, and/or load hatches that are configured for the loading of waste material into, or the removal of non combustible materials and ash from, the gasification chamber, and which may provide access to the inner portion for service and maintenance purposes.

Additionally, the exterior vessel includes structural components, such as metal hangers, from which insulation materials may be operably attached to the inner surfaces of the exterior vessel walls. Insulation materials are preferably configured to assist in maintaining operating temperatures within the gasification chamber during the gasification process, while also protecting the walls of the exterior vessel from prolonged exposure to excessive heat.

[0033] The insulation materials are preferably comprised of multiple layers of spun ceramic fiber and hard ceramic board. The use of ceramic fiber and board allows the gasification chamber to cool down faster than prior designs that rely on refractory brick style materials.

This faster cool down period decreases the lapse in time between the gasification of subsequent loads of waste materials. Such ceramic insulation material is preferably designed to contain the heat of the process within the inner portion of the gasification chamber, and to prevent the exterior vessel wall surface temperature from rising above 150 degrees F. Furthermore, because ceramic insulation materials are considerably lighter than refractory brick style materials, the supporting hangers and exterior vessel walls may be constructed from lighter materials, thereby decreasing material and fabrication costs. In the illustrated embodiment of the present invention, the inner surfaces of the exterior vessel walls and attached insulation materials, preferably define the area of the inner portion.

[0034] Inside the inner portion of the gasification chamber is a mesh liner. The liner is preferably constructed from stainless steel mesh screen that is oriented to create a basket configuration around the sides of the loaded waste material. The liner is preferably supported approximately three inches away from the side walls and the floor by an additional set of hangers, or pins, the hangers preferably being welded to the walls of the exterior vessel and protrude through the ceramic insulation material. Supporting the liner away from the sidewalls and floor of the exterior vessel, and thus preventing the direct physical contact of said waste material with the walls of exterior vessel, allows the gasification chamber walls to be fabricated from substantially thinner material, thereby reducing the weight and associated expenses of fabricating and transporting the mobile gasification unit.

The base of the loaded waste material is preferably supported by a pipe bridge floor assembly or other such means that prevent said loaded waste from being positioned directly on the floor of the gasification chamber.

[0035] Supporting the loaded waste material away from the walls and floor of the gasification chamber allows process gas to freely flow around the top, sides, and bottom of said loaded waste material. Furthermore, the plurality of openings in the mesh screen of the liner and the spacing of the supporting bridge floor assembly

allows the process gas to flow into the sides and bottom of the basket, thereby increasing the surface area of waste materials that are exposed to process gas, and thus creates primary reaction zones along said sides, bottom, and top of the loaded waste material. Because gasification cycle time is a function of waste material surface area that is exposed to process gases, these elements of the design allow for a significant reduction in the process cycle time and temperatures. Reduced gasification temperatures and time also decrease the lapse in time before a subsequent load of waste material may undergo the gasification procedure.

[0036] At least one heating device is operably connected the gasification chamber.

The at least one heating device is configured to provide a source for initiating the gasification procedure and may assist in maintaining gasification operation temperatures within the gasification chamber. In the illustrated embodiment of the present invention, the at least one heating device may include, but is not limited to, a fuel-fired burner or an electric thermal radiant heat assembly, and may also be configured to provide an ignition source for the combustion of produced fuel gas in the produced fuel gas combustion chamber. In one embodiment of the illustrated invention, the at least one heating device is comprised of electric heating elements that are operably connected to the chamber via two penetrations that are positioned along at least one wall of the gasification chamber.

[0037] At least one process gas inlet is operably positioned and configured to allow process gas to enter the inner portion of the gasification chamber. The process gas may be comprised of, but is not limited to, ambient air, a high oxygen content gas such as raw oxygen, or some combination thereof. The at least one process gas inlet is preferably fitted with a valve or damper so that process gas enters into the gasification chamber at a controlled rate. A controller, such as, but not limited to, a process logic controller, preferably located in a control room or on a control board, may be used to monitor the environment in the gasification chamber, including oxygen and temperature levels, and use such information in determining whether the valve for the at least one process gas inlet should be opened or closed.

[0038] While the process gas may be comprised of ambient air, in the illustrated embodiment of the present invention, any supplemental process gas that is vented

into the inner portion is preferably a high oxygen content gas, such as, but not limited to raw oxygen or a raw oxygen-ambient air mixture. Because nitrogen comprises approximately 78% of ambient air, the use of a high content oxygen gas in lieu of ambient air typically translates into the need to transport, and the presence of, a smaller volume of process gas in order to obtain desired oxygen levels than would be required if ambient air were used. The reduction in the volume of process gas that must be transported to, and present in, the gasification chamber, allows for a reduction in size of the duct work that transports the process gas. This reduction in size may reduce both material and fabrication costs while also decreasing the weight of the system. Furthermore, the use of high oxygen content gases, such as, but not limited to, raw oxygen, rather than ambient air also preferably decrease the formation and release of regulated pollutants, such as nitrous oxides.

[0039] At least one temperature sensor is positioned within the inner chamber to monitor temperature before, during, and after the gasification process.

Temperature information detected by the at least one temperature sensor is preferably relayed to the control room. During the gasification process, such information obtained by the at least one temperature sensor may be used by the controller to determine whether the at least one heating device should be activated or deactivated, and whether the at least one process gas inlet should be opened or closed. In the illustrated embodiment of the present invention the temperature sensors are six Type-K thermocouples that are positioned along the mid-line of the chamber, with three on each side of two parallel walls.

[0040] The present invention also includes at least one outlet orifice that is positioned along a portion of an exterior vessel wall and at least one inlet orifice positioned along at least a portion of the produced fuel gas combustion chamber.

The at least one outlet orifice preferably provides a passageway for produced gases to be removed from the gasification chamber, while the at least one inlet orifice preferably provides a passageway for said gases to pass into the produced fuel gas combustion chamber. Both the at least one outlet and inlet orifice are preferably configured for operable attachment to an induced draft fan. Through the opening of the at least one inlet orifice, the fan preferably provides pressurization to the

produced fuel gas combustion chamber so that produced fuel gases that are produced during the gasification process are withdrawn out from the gasification chamber, through the opened at least one outlet, and into the produced fuel gas combustion chamber. The at least one outlet orifice may be fitted with a gate valve that can be employed to regulate the exit of produced fuel gas from the gasification chamber.

[0041] In one embodiment of the present invention, the produced fuel gas combustion chamber is a maze ignition chamber that is comprised of an insulated enclosure, the enclosure having an exhaust port, an outer surface, and an inner chamber. Although the present invention is capable of operating with only one maze ignition chamber, in accordance with the illustrated embodiment of the present invention, each of the at least one gasification chambers has a dedicated maze ignition chamber. Within the inner chamber of the enclosure is preferably at least one baffle and at least one produced gas igniter, the at least one baffle being oriented to create a winding passageway in the inner chamber. In accordance with the illustrated embodiment of the present invention, the at least one inlet orifice is operably positioned so that produced fuel gases that are withdrawn and/or vent from the gasification chamber may flow into the inner chamber of the enclosure.

Furthermore, in the illustrated embodiment of the present invention, at least a portion of the container top and base preferably form at least a portion of the walls of the enclosure. Additionally, the maze ignition chamber may be positioned so that at least a portion of one sidewall of the enclosure is also at least a portion of an exterior vessel sidewall.

[0042] After passing through the at least one inlet orifice and into the inner chamber of the maze ignition chamber, supplemental flare gas is preferably added to the produced fuel gas via a supply nipple so as to improve the combustibility of the produced fuel gas. Alternatively, supplemental flare gas may be added to the produced fuel gas after being withdrawn from the gasification chamber but prior to passage into the produced fuel gas combustion chamber. Although the supplemental flare gas may be comprised of ambient air, in the illustrated embodiment of the present invention, the supplemental flare gas is a high oxygen content gas, a high hydrogen content gas, or some combination thereof. The

produced fuel gas and supplemental flare gas then preferably proceed onto the at least one produced gas igniter, whereupon the gases are combusted. Once combusted, the gases proceed through the winding passageway.

[0043] The at least one baffle within the inner chamber is oriented so as to create a winding passageway through which the combusting produced fuel gases may flow.

In the illustrated embodiment of the present invention, the at least one baffle is preferably oriented so as to subject the flowing gases to square turns. This winding passageway creates additional turbulence that enhances the mixing of the combusted gases. Each turn in the winding passageway that is created by the at least one baffle also allows for additional retention time of the combusting gases in the hot environment of the maze. In the illustrated embodiment of the present invention, the additional retention time allows the combusted gases to continue to be exposed to an environment of approximately 1550-1750 degrees F.

Combusted gases exiting the maze chamber via the exhaust port are preferably used to provide heat to a primary end use device, such as, but not limited to, a boiler, so as to provide energy for steam or hot water production in lieu of natural gas.

[0044] In an alternative embodiment of the present invention, the produced fuel gas combustion chamber is a gas accumulation tank that is preferably located adjacent to the partitioning wall. In such an embodiment, uncombusted produced fuel gases are stored in the gas accumulation tank before being delivered to a primary end use device. In an effort to retain the high temperatures of the accumulated produced fuel gas, the gas accumulation tank is preferably encapsulated in a blanket of insulation material, such as a ceramic material. The gas accumulation tank also preferably includes at least one pipe flange that pierces through the exterior of the container. The at least one flange serves as a gas delivery port from which the produced fuel gas product to one or more end use devices. In the illustrated embodiment of the present invention, the combustion of the produced fuel gases preferably occurs at some point after the produced fuel gases have passed through the gas accumulation tank and have been delivered to the primary end use device.

[0045] The present invention may also include at least one water line. Such a water line may be configured to provide an emergency quench for the process as well as dust control during the clean-out process. In one embodiment of the present invention, the at least one water line is comprised of two water lines that pierce the partitioning wall that divides the gasification chamber from the remainder of the interior of the mobile gasification unit, the two water lines connecting a water supply pump and pressure unit located in the control room to the spray nozzles located in the ceiling of the gasification chamber. In another embodiment, the water supply pump and pressure unit are located outside of the mobile gasification unit.

BRIEF DESCRIPTION OF SEVERAL VIEWS OF THE DRAWINGS [0046] For a more complete understanding of this invention, reference should now be made to the embodiment illustrated in greater detail in the accompanying drawings and described below by way of example of the invention.

[0047] Figure 1 illustrates a perspective view of a mobile gasification unit with fan housings in accordance with the illustrated embodiment of the present invention.

[0048] Figure 2 illustrates a top view of a mobile gasification unit in accordance with the illustrated embodiment of the present invention.

[0049] Figure 3 illustrates a top interior cross sectional view of a mobile gasification unit in accordance with the illustrated embodiment of the present invention.

[0050] Figure 4 illustrates a rear side view of a mobile gasification unit in accordance with the illustrated embodiment of the present invention.

[0051] Figure 5 illustrates a front side view of a mobile gasification unit in accordance with the illustrated embodiment of the present invention.

[0052] Figure 6 illustrates a side view of a mobile gasification unit in accordance with the illustrated embodiment of the present invention.

[0053] Figure 7 illustrates a top view of a mobile gasification unit in accordance with an alternative embodiment of the present invention.

[0054] Figure 8 illustrates a top interior cross sectional view of a mobile gasification unit in accordance with an alternative embodiment of the present invention.

[0055] Figure 9 illustrates a side partial cross sectional view of a mobile gasification unit in accordance with one embodiment of the present invention.

[0056] Figure 10 illustrates a maze ignition chamber in accordance with the illustrated embodiment of the present invention.

[0057] Figure 11 illustrates a cross sectional side view of insulation material used in accordance with the illustrated embodiment of the present invention.

[0058] Figure 12 illustrates a partial cross sectional view of a gasification chamber in accordance with the illustrated embodiment of the present invention.

[0059] Figure 13 illustrates a cross sectional view of a fuel gas extraction assembly in accordance with the illustrated embodiment of the present invention.

DETAILED DESCRIPTION OF THE INVENTION [0060] Figures 1 and 9 illustrate a mobile gasification unit 10 in accordance with one embodiment of the present invention. The gasification unit 10 is comprised of a container 11, at least one gasification chamber 12a, 12b, and at least one produced fuel gas combustion chamber 16a, 16b. Furthermore, as illustrated in Figure 8, the mobile gasification unit 10 may also be configured to include a control room 14. The container 11 is preferably comprised of a plurality of side walls 22a, 22b, 22c, 22d, a base 24, and a top portion 26. In the illustrated embodiment of the present invention, the container 11 is, or is of similar construction to, a standard sea cargo shipping container, which is approximately eight feet in width, nine feet in height, and twenty, forty, or forty-two feet in length. These dimensions however may change to satisfy waste capacity and/or gasification requirements.

[0061] Furthermore, the size and number of the at least one gasification chamber 12a, 12b may be impacted by the choice of process gas. For instance, the use of process gases that has large amounts of undesirable gases accompanying the desired oxygen, such as the high content of nitrogen present in ambient air,

requires that the at least one gasification chamber 12a, 12b be sized to accommodate the inclusion of the undesired gases. However, in the illustrated embodiment of the present invention, the process gas is preferably comprised of a high oxygen content gas, such as, but not limited to, raw oxygen. While the present invention will operate using ambient air, which includes a large volume of undesirable nitrogen, the use of a high oxygen content gas, such as raw oxygen, which reduces or eliminates the inclusion of undesirable gases, may allow for a decrease in the required size of the at least one gasification chamber 12a, 12b.

[0062] Each of the at least one gasification chambers 12a, 12b have an exterior vessel 30a, 30b and an inner portion 32a, 32b. The exterior vessel 30a, 30b is preferably configured so that at least a substantial portion of the at least one gasification chamber 12a fits into the interior of the container 11. The exterior vessel 30a, 30b for the at least one gasification chamber 12a, 12b is comprised of a plurality of side walls, a top portion, and a base. In the illustrated embodiment of the present invention, at least a portion of the sidewalls 22a, 22b, 22c, 22d, base 24, and top portion 26 of the container 11 that are adjacent to the gasification chamber 12a, 12b are used as at least a portion of the plurality of walls of the exterior vessel 30a, 30b, as illustrated in Figures 2,3, 8, and 9. Alternatively, the exterior vessel 30a, 30b for each of the at least one gasification chamber 12a, 12b may be comprised of walls that are substantially dedicated for that individual chamber 12a, 12b.

[0063] In the illustrated embodiment of the present invention, each exterior vessel 30a, 30b, also includes a partitioning wall 23a, 23b within the container 11 that substantially separates the at least one gasification chamber 12a, 12b from the remainder of the inner portion of the container 11, as illustrated in Figures 3,8, and 9. The location of the partitioning wall 23a, 23b within the container 11 is preferably determined by the total waste processing volume desired. For example, if need dictates a two ton (15 cubic yard) waste capacity, then preferably one half of a container 11 having the equivalent size of a conventional twenty foot sea cargo container is used for a gasification chamber 12a.

[0064] The remainder of the container 11 that is separated from the at least one gasification chamber 12a by the partitioning wall 23a is designed to house at least

one produced fuel gas combustion chamber 16 and either an additional gasification chamber 12b or, alternatively, a control room 14, as illustrated in Figures 3,8, and 9. In an embodiment in which the container 11 includes a control room 14, the control room 14 may be configured to include various controls, such as, but not limited to, a process logic controller 98, which is used to control gasification conditions, including the gas content and temperature inside the at least one gasification chamber, a primary access loading door 38a, a recovery removal door, a hydraulic assembly 71a, water pump and pressure unit 62 and associated spray systems, temperature and gas sensing equipment, and control devices. Access to the control room may be obtained via an access door 36b. In the illustrated embodiment of the present invention, the access door 36b is comprised of two adjacent hinged doors that are both sections of a container 11 sidewall 22d, as illustrated in Figure 8.

[0065] The exterior vessel 30a, 30b of the at least one gasification chamber 12a, 12b also includes a primary access loading door 38a, 38b that is configured to cover at least one opening along the top portion 26 of the container 11, and when in an opened position, allows for the insertion of waste material into the inner portion 32a, 32b of the at least one gasification chamber 12a, 12b. In the illustrated embodiment of the present invention, the opening and closing of the primary access loading door 38a, 38b is accomplished by the use of a hydraulic assembly 71a, 71b that is operably connected to the primary access loading door 38a, 38b. In one embodiment of the present invention, a seal is operably position between the base of the primary access loading door 38a, 38b and the container 11, which is configured to create an air-tight fit between the primary access loading door 38 and the exterior vessel 30. The primary access loading door 38a, 38b may also include a safety pressure relief vent 112a, 112b that is designed to dislodge or"burp"in the event that the pressure within the at least one gasification chamber 12a, 12b reaches undesirable levels (usually 4 to 6 psi).

[0066] The exterior vessel 30a, 30b in the illustrated embodiment of the present invention also preferably includes at least one access door 36a, 36b for the removal of noncombustible material, as illustrated in Figures 2,3, 7, and 8. The at least one access door 36a, 36b is also preferably configured to provide access to the inner

portion 32a, 32b for maintenance and service purposes. In the illustrated embodiment of the present invention, the access door 36a, 36b is comprised of two adjacent hinged doors that are both preferably sections of the container sidewall 22c, 22d, as shown in Figure 6. A seal is preferably used to insure an air-tight fit between the at least one access door 36a, 36b and the container 11 when the at least one access door is in a closed position.

[0067] In the illustrated embodiment, the exterior vessel 30a, 30b also includes at least one disposal opening positioned along the base 24 of the container 11 to aid in the removal of post-process residual materials from the at least one gasification chamber 12a, 12b. In the illustrated embodiment of the present invention, the disposal opening is preferably a rectangular slot, measuring approximately 12 inches wide by 14 inches long, and is configured to allow for residual ash and small pieces of residual material to be flushed out of the chamber during a clean- out process.

[0068] Figures 2,8, and 9 illustrate the inner portion 32a, 32b of the at least one gasification chamber 12a, 12b in accordance with one embodiment of the present invention. At least a portion of the surrounding inner surfaces of exterior vessel 30a, 30b walls 22a, 22b, 22c, 22d, 23a, 23b, base 24, and top portion 26 are lined with insulation material 49 to assist in maintaining the temperature of the inner portion 32 during the gasification procedure and/or to protect the structure of the at least one gasification chamber 12a, 12b from prolonged exposure to excessive heat. As illustrated by Figures 11 and 12, metal hangers 66 that are operably attached to the inner portion of the walls 22a, 22b, 22c, 22d, 23a, 23b of the exterior vessel 30a, 30b are used to line at least a portion of said walls 22a, 22b, 22c, 22d, 23a, 23b with an approximately eight inch thick layer of insulation material 49. In accordance with one embodiment of the present invention, the insulation material 49 is preferably comprised of three layers of spun ceramic fiber 50 and hard ceramic board 52. Such insulation material is preferably designed to contain the heat of the gasification process, while preferably also limiting the temperature of the outer surfaces of the container 11 walls 22a, 22b, 22c, 22d, 23a, 23b, 24,26 to a temperature of no greater than 150 degrees F. Furthermore, such insulation material 49 preferably has the ability to cool down relatively quickly so

as to assist in allowing a faster cool down period of the inner portion 32a, 32b following the completion of a gasification procedure. In the preferred embodiment of the present invention, the hangers 66 are welded to the interior of the exterior vessel walls 30 sidewalls 22a, 22b, 22c, 22d, 23a, 23b and are approximately 6 inches in length. Once in place, the insulated materials 49 are preferably pushed over the welded hangers 66.

[0069] The present invention also preferably includes at least one temperature sensor 40, such as a thermocouple, and at least one oxygen sensor 96 to monitor the temperature and oxygen levels within the inner portion 32a, 32b, as illustrated in Figure 12. Information regarding temperature and oxygen levels inside the inner portion 32a, 32b, as detected by a the sensors 40,96, are preferably sent to the controller 98. Such information may then indicate to the controller 98 whether an action is needed, such as whether the heating device 114 should be activated or deactivated. In the illustrated embodiment of the present invention, six Type K thermocouples are used to detect whether the average ambient temperature in the inner portion 32a, 32b has reached, or is within, a predetermined range of operating temperatures. These thermocouples may be positioned in a variety of locations, including, but not limited to, the placement of three thermocouples 40 along the mid line of opposing gasification chamber 12a, 12b sidewalls 22a, 22b.

[0070] At least one process gas inlet 116 is configured to release process gas into the inner portion 32a, 32b of the at least one gasification chamber 12a, 12b. While process gas that passes through the at least one process gas inlet 116 may take the form of ambient air, the at least one process gas inlet 116 is preferably operably connected to a source for high oxygen content gas, such as, but not limit to, raw oxygen. In one embodiment of the present invention, the high oxygen content gas is supplied by an oxygen generator. However, oxygen may also be provided from other sources, such as a pre-bottled cylinder of oxygen. In the illustrated embodiment of the present invention, the at least one process gas inlet 116 is comprised of six four inch diameter pipe nipples that are positioned along the lower quadrant of one side of the at least one gasification chamber 12a, 12b. The at least one process gas inlet 116 is also preferably operably connected to a valve, the valve being used to control the rate at which process gas enters into the at least

one gasification chamber 12a, 12b. The valve is preferably connected to a motor, the motor being operably connected to the controller 98, so that, as the controller 98 monitors and regulates oxygen and temperature levels within the inner portion 32 of the at least one gasification chamber 12a, 12b, the controller 98 may send signals to the motor as to whether the valve should be in an opened or closed position depending on the temperatures and oxygen levels within the gasification chamber 12a.

[0071] As shown in Figures 9 and 12, the present invention also includes a mesh liner 58 and supporting bridge floor assembly, including, but not limited to, support rails 92, that are configured to hold waste material within the inner portion 32a, 32b of the at least one gasification chamber 12a, 12b and away from the sidewalls and floor of the exterior vessel 30a, 30b, as illustrated in Figures 3,8, 9, and 12. The rails 92 are preferably configured with a sufficient space between adjacent rails 92 so as to allow process gas to flow, and residual ash and remaining non-combusted materials to fall, between the rails while also preventing loaded waste material from falling to the base of exterior vessel 30. Although the liner 58 may be configured to create a number of different orientations, such as, but not limited to, a basket or bowl type orientation, in the preferred embodiment of the present invention, the liner 58 has a generally rectangular configuration.

[0072] The mesh liner 58 is preferably supported by a plurality of pins 80 that are operably connected to a portion of the adjacent exterior vessel 30 walls 22a, 22b, 22c, 22d, 23a, 23b, as illustrated in Figure 12. In the illustrated embodiment of the present invention, the mesh liner 58 is constructed from panels of 316 stainless steel mesh, the mesh having a wire diameter of 1/4 inch and hole diameter of two inches. Furthermore, in the illustrated embodiment of the present invention, the pins 80 are preferably about 12 inch long, 3/4 inch diameter stainless steel bolts, with the heads of said bolts being welded to the interior of the exterior vessel 30 sidewalls 22b, 22c, 22d, 23a, 23b. In such an embodiment, about 9 bolts are preferably present per 3 foot x 10 foot mesh panel. The mesh liner 58 is preferably secured to the threaded ends of the bolts via a set of double nuts and fender washers. The support rails 92 are preferably comprised of two inch diameter pipes laid in rows with adequate spacing so as to allow process gas to

flow into the bottom of loaded waste material, and are approximately ten inches above the floor of the exterior vessel 30a, 30b so as to provide sufficient clearance for the gasification environment.

[0073] The mesh liner 58 is preferably offset away from the insulation material 49 that is attached to the inner portion of the adjacent exterior vessel 30 walls 22a, 22b, 22c, 22d, 23a, 23b. In the illustrated embodiment of the present invention, the mesh liner 58 is positioned approximately 3 inches away from said insulation material 49. By offsetting the mesh liner 58 away from the adjacent walls 22a, 22b, 22c, 22d, 23a, 23b, process gas may circulate around the liner 58 and through the mesh openings on the bottom and sides of said liner 58, thereby directly exposing a substantial portion of the waste material that is located in proximity to the bottom, sides, and top of the liner 58 to process gas. This increase in surface area of said collected waste material that is exposed to process gases results in an increase in the size of the primary reaction zone, and thereby allows for both a significant reduction in both gasification process cycle time and required gasification temperatures.

[0074] Additionally, because waste material is placed within the constraints of the mesh liner 58, and is not against the walls adjacent walls 22a, 22b, 22c, 22d, 23a, 23b of the exterior vessel 30, the walls of the at least one gasification chamber 12a, 12b preferably do not come into direct physical contact with said waste material.

By preventing the direct physical contact of said waste material with the walls 22a, 22b, 22c, 22d, 23a, 23b of the at least one gasification chamber 12a, 12b, the exterior vessel 30 walls 22a, 22b, 22c, 22d, 23a, 23b, 24,26 may be fabricated from substantially thinner material, thereby reducing the weight and associated expenses of fabricating the at least one gasification chamber 12a, 12b.

Furthermore, offsetting the liner 58 away from the exterior vessel 30a, 30b walls 22a, 22b, 22c, 22d, 23a, 23b, 24 prevents waste material from covering the at least one process gas inlet 116 and blocking the flow of process gas into the inner portion 32a, 32b.

[0075] At least one heating device 114 is operably connected to the inner portion 32a, 32b of the at least one gasification chamber 12a, 12b. The at least one heating device 114 is preferably configured to provide heat to the inner portion 32a, 32b

for initiation of the gasification process and any additional heat that may be required during the gasification process so that the temperature within the inner portion 32a, 32b remains within a desired operating range. The at least one heating device 114 may be comprised of, but is not limit to, a fuel-fired burner or an electric thermal radiant heat assembly. Furthermore, in one embodiment of the present invention, a hydrogen generator may provide a combustible hydrogen gas to the at least one heating device 114 that may be used to provide a live flame in the gasification chamber or in the produced fuel gas combustion chamber. In the illustrated embodiment of the present invention, the at least one heating device 114 is comprised of a plurality of electric radiant heat elements that lay on top of the supporting rails 92, as illustrated in Figure 12. With such an embodiment, an additional heating element may be added between the support rails 92 and the floor so as to ensure the complete oxidation of any combustible waste material that may have fallen between the spacing of the rails 92. In an alternative embodiment of the present invention, two penetrations in the exterior vessel 30 partitioning wall 23a, 23b provides attachment and access for electric heating elements which maintain temperature with the inner portion 32a, 32b at desired levels. In another embodiment of the present invention, the at least one heating device 114 is a comprised of a plurality of electric heating elements that located in the fuel chamber 16 and which also provide ignition for the combustion of produced heavy fuel gases in said fuel chamber 16.

[0076] The illustrated embodiment of the present invention may also include at least one emergency water line 56a, 56b, as shown in Figure 8. The at least one emergency water line 56a, 56b is preferably comprised of two one inch diameter water lines that pierce the portioning wall 23a, 23b of an exterior vessel 30a, 30b, and are configured to provide emergency quench for the gasification process and dust control during the clean-out process. In one embodiment of the present invention, the at least one emergency water line 56a, 56b operably connects a water supply pump and pressure unit 62 located in the control room 14 to the spray nozzles located in the ceiling of the gasification chamber 12, the inlet 61 of said pump and pressure unit 62 being operably connected to a water source, such as, but not limited to, a hydrant or water supply line.

[0077] Figures 13 illustrates a fuel gas extraction assembly 100 in accordance with the illustrated embodiment of the present invention. An induced draft fan 102 is operably connected to the inner portion 32 of the at least one gasification chamber 12 and the produced fuel gas combustion chamber 16. In the illustrated embodiment, the at least one outlet orifice 82 provides a passageway in which produced fuel gases may be vented or withdrawn from the inner portion 32 of the at least one gasification chamber 12, while the at least one inlet orifice 84 provides an inlet for the vented produced fuel gases to enter into the produced fuel gas combustion chamber 16. The fan 102 is preferably configured to create a pressure in the produced fuel gas combustion chamber 16 that assists in withdrawing the produced fuel gas out from the at least one gasification chamber 12 and into produced fuel gas combustion chamber 16. In the illustrated embodiment of the present invention, the inlet and outlet orifices 82,84 are 24 inch square flanged openings that penetrate the top portion 26 of the container 11. Furthermore, the at least one outlet orifice 82 is operably connected to a gate valve 104 that is configured to regulate the removal of produced fuel gases out of the at least one gasification chamber 12. In the illustrated embodiment, the gate valve 104 is a damper that is operably connected to an electric motor 106 that controls the movement of the damper. Furthermore, in the illustrated embodiment, the fan 102 is preferably a squirrel cage blower fan constructed from stainless steel that is powered by a five horsepower variable speed motor and has a housing 86 that is constructed from 1/4 inch thick 316 stainless steel that is configured to resist the high temperatures of incoming produced fuel gases. As shown in Figure 13, the housing 86 may be operably connected to a fan 108 that may provide a supplemental flare gas, including, but not limited to, ambient air, a high oxygen content gas such as raw oxygen, a high content hydrogen gas, or a combination thereof, to the stream of withdrawn produced fuel gas prior to arrival into the produced fuel gas combustion chamber 16. However, in an alternative embodiment, the produced fuel gas combustion chamber 16 is configured to supply the supplemental flare gas may be into the stream of produced fuel gas after said produced fuel gas passes through the inlet orifice 84, as discussed below.

[0078] Although Figure 13 illustrates the fuel extraction assembly 100 in conjunction with a maze ignition chamber 70, the illustrated fuel extraction assembly 100 may also be configured for use in conjunction with a gas accumulation tank 48, as illustrated in Figure 8. In such embodiments, because produced fuel gases are preferably not combusted until after leaving the gas accumulation tank 48, the fuel extraction assembly 100, when used with said tank 48, does not have to be operably connected to a fan 108 that introduces a oxygen or hydrogen containing gas into the passing stream of withdrawn produced fuel gases in the fuel extraction assembly 100.

[0079] As shown in Figure 8, in an alternative embodiment, the outlet orifice 82a is operably connected to a flange 34 that is preferably eight inches in diameter and is configured to be operably connected to the induced draft fan 102 and housing 86a, and which is preferably fitted with a gate valve 104. The gate valve 104 allows for the regulated removal of produced fuel gases from the at least one gasification chamber 12a, 12b and into an intake portion of the produced fuel gas combustion chamber 16. In such an embodiment, the flange 34 is preferably positioned along a sidewall 22a of the exterior vessel 30a. However, the flange may also be positioned along the top portion 26 of the container 11.

[0080] In accordance with one embodiment of the present invention, the produced fuel gas combustion chamber 16 receives withdrawn or vented produced fuel gases from the gasification chamber 12 for combustion and/or storage before delivery to a primary end use device, such as, but not limited to a boiler. In the preferred embodiment of the illustrated invention, the produced fuel gas combustion chamber 16 is a maze ignition chamber 70 as illustrated in Figures 3,9, and 10.

Although a single maze ignition chamber 70 may, in some situations be sufficient to support multiple gasification chambers 12a, 12b, in accordance with the illustrated embodiment of the present invention, each gasification chamber 12a, 12b has its own dedicated maze ignition chamber 70a, 70b, each dedicated maze 70a, 70b preferably mutually sharing at least one common wall with the associated gasification chamber 12a, 12b, as illustrated in Figures 3 and 9.

[0081] The maze ignition chamber 70a is capable of being used when the unit 10 includes more than one gasification chamber 12a, 12b or with embodiments that

include a control room 14. For example, in the illustrated embodiment, when a section of the container 11 includes a control room 14, one maze 70 sidewall is preferably used to separate the maze 70a and gasification chamber 12a from the control room. For configurations in which an additional gasification chamber 12b replaces the control room, the dedicated maze chambers 70a, 70b are preferably spaced approximately 12 inches from one another by an insulated divider 94. In the illustrated embodiment, the divider 94 preferably serves as a common wall for both maze chambers 70a, 70b.

[0082] Figure 10 illustrates a cross sectional side view of the maze chamber 70a in accordance with the illustrated embodiment of the present invention. The maze chamber 70a is preferably comprised of insulation 49, an enclosure 75, an inner chamber 74, at least one inlet orifice 84a, 84b, at least one baffle 76, at least one secondary igniter 78, and at least one exhaust port 88. At least a portion of the base 24 and top portion 26 of the container 11 are used as a portion of the walls for the enclosure. The at least one baffle 76 is oriented to so as to create a winding passageway in the inner chamber 74 of the chamber 16 through which produced fuel gas may flow along while passing from the inlet orifice 84a and out through the exhaust port 88a. Each turn in the winding passageway that is created by positioning of the at least one baffle 76 not only creates turbulence so as to aid in mixing the passing gases, but also allows for additional retention time of those gases in the hot environment of the maze 70a enclosure 75. In the illustrated embodiment of the present invention, the additional retention time in the enclosure 75 allows the gases to continued to be exposed to an environment of approximately 1550-1750 degrees F.

[0083] In accordance with the illustrated embodiment of the present invention, once within the inner chamber 74, the produced fuel gases are preferably mixed with a supplemental flare gas, such as, but not limited to, ambient air, a high oxygen content gas or a high hydrogen content gas, so as to improve the combustibility of said produced fuel gases In the illustrated embodiment of the present invention, the supplemental flare gas enters into the winding passageway via a 3/4 inch nipple 110 located above the first of the at least one produced gas igniter 78 and beneath the at least one inlet orifice 84a. In one embodiment of the

present invention, hydrogen may be supplied via a hydrogen generator or a hydrogen supply tank. Supplemental flare gas is preferably added to the produced fuel gas at a controlled rate, as determined by the process controller 98. However, as previously discussed, the mixing of the supplemental flare gas with the produced fuel gas may occur prior to passage through the inlet orifice 84a.

[0084] The mixing of supplemental flare gases in the form of high oxygen or hydrogen content gases with the produced fuel gas may reduce the potential for the formation of regulated pollutants. Furthermore, because high oxygen content gas, such as, but not limited to raw oxygen, or high hydrogen content gases, or a combination thereof, preferably contain less undesirable gas volume than ambient air, the duct work required for transporting the high oxygen or hydrogen content gases to the maze chamber 70, and the maze chamber 70 itself, may have a smaller overall size then if the less desirable gas, such as ambient air, were used. The use of such relatively clean burning gases as the supplemental flare gas may also increase the size of the"fireball"that is created during combustion, which thereby further improves the mixing of the produced fuel gas with the supplemental flare gas.

[0085] As the mixed supplemental flare gas and produced fuel gas proceed along the maze 70a, the gases encounter the first of the at least one produced gas igniter 78, the at least one produced gas igniter 78 being configured to provide a source for the combustion of the produced fuel gas and supplemental flare gas. The at least one produced gas igniter 78 may be comprised of, but is not limit to, a fuel- fired igniter or an electric thermal radiant heat assembly. In the illustrated embodiment of the present invention, the at least one produced gas igniter 78 is comprised of three to four sets of electric radiant heat panels that have a generally "W"shaped configuration and which are approximately 24 inches high by 24 inches long, as illustrated in Figure 3. In an alternative embodiment, the at least one produced gas igniter 78 may be comprised of four electric heat elements that are enclosed in stainless pipe and covered with a piece of titanium expanded metal with 1/8 inch openings and which are preferably heated by the passing of a 220 volt current through said electric heat element.

[0086] The maze chamber 70a may also include at least one access door 90a. In the preferred embodiment of the present invention, the access door 90a provides a point of entry for maintenance of the maze chamber 70a and/or service of the at least one produced gas igniter 78. In the illustrated embodiment of the present invention, the at least one access door 90a is preferably located on one sidewall of both the maze chamber 70a and container 22a.

[0087] In an alternative embodiment, the produced fuel gas combustion chamber 16 is comprised of a gas accumulation tank 48. In such an embodiment, the gas accumulation tank 48 preferably includes at least one inlet orifice 84a that is operably connected to the at least one gasification chamber 12a via at least one exhaust manifold 62, the at least one exhaust manifold 62 being operably connected to the induced draft fan 102 and flange 34, as illustrated in Figure 8.

The induced draft fan 102 preferably provides pressurization to the gas accumulation tank 48, thereby assisting in venting and/or withdrawing the produced fuel gas through the at least one outlet orifice 82a. Produced fuel gases are stored and eventually delivered from the gas accumulation tank 48 to the appropriate primary end use device, such as, but not limited to, water heaters, boilers, chillers, kiln dryers, et al for subsequent combustion.

[0088] In accordance with this illustrated embodiment of the present invention, the size and configuration of the gas accumulation tank 48 is preferably determined based on the size and capacity requirements of the at least one gasification chamber 12a, 12b and the available space in the container 11. The gas accumulation tank 48 is preferably a round, square, or rectangular tank that is approximately four feet in diameter and approximately eight feet six inches in height, and which is wrapped in twelve inches of a ceramic isolative blanket. The gas accumulation tank 48 is also preferably located adjacent to the flange 34, inside the control room 14.

[0089] In the illustrated embodiment of the present invention, at least one pipe flange 118 is welded into the side of the gas accumulation tank 48, the opposite end of the at least one flange 118 preferably piercing the exterior of the container 11. The at least one pipe flange 118 serves as gas delivery port through which the

produced fuel gas fuel product produced in the at least one gasification chamber 12a, 12b is distributed to the primary end use devices.

[0090] Operation of the mobile gasification unit 10 begins with transporting the unit 10 to a desired location. For ease of mobility, the unit 10 is preferably constructed to have a standard container 11 configuration, such as a sea cargo container configuration, so that the unit 10 may be transported via standard modes of transportation, including, but not limited ship, truck, or train= Once at the desired location, the gasification unit 10 may remain on the transportation device, such as a truck bed, or may be set down upon a stable surface, such as, but not limited to, concrete or a prepared bed of gravel.

[0091] Operation of the gasification unit 10 in accordance with the illustrated embodiment of the present invention typically begins with waste material entering though the opened primary access door 38a and into the inner portion 32 of the at least one gasification chamber 12a, 12b. The waste material is then placed onto the support rails 92 and into the mesh liner 58 that is supported by metal pins 80 and which extends away from a portion of the inner surfaces of the adjacent exterior vessel 30a, 30b walls 22a, 22b, 22c, 22d, 23a, 23b. Once the waste material is loaded into the mesh liner 58, the primary access door 38 and any other additional exterior vessel 30a, 30b removal ports or doors 36a, 36b are subsequently closed.

[0092] An air purge is then employed in which ambient air is vented out from the inner portion 32 so as to reduce the volume of oxygen in the at least one gasification chamber 12a, 12b. During the air purge process, the valve for the at least one process gas inlet 116 is shut closed so as to prevent additional ambient air from entering into the at least one gasification chamber 12a, 12b. The closing of the at least one process gas inlet 116 may be initiated by a signal that is sent from a controller 98 in the control room 14 or on the control board, to the motor that opens and closes said valve. Preferably, an induced draft, such as the fan 102 that is operably connected to the outlet orifice 86a, 86b is then activated to withdraw ambient air out from the chamber 12a, 12b until oxygen levels and air volume within the at least one gasification chamber 12a, 12b have been reduced to desired levels for the initiation of the gasification process.

[0093] Once oxygen levels and air volume within the inner portion 32 of the at least one gasification chamber 12a, 12b are reduced to desired levels, the at least one heating device 114 is activated, and remains activated until the temperature within the inner portion 32 reaches a desired gasification temperature, as detected by the at least one temperature sensor 40. The at least one heating device 114 may also provide the heat required to sustain an optimal gasification environment.

[0094] As the temperature within the inner portion 32 reaches desired gasification levels, the valve for the at least one process gas inlet 116 may be opened. The opening of the at least one process gas inlet 116 occurs in a controlled manner, as determined by the controller 98, so that the desired gasification temperatures and oxygen levels are maintained, while also preventing the possibility that combustion will occur. Typically, the gasification of solid, sludge, and liquid wastes happens in a controlled atmosphere of restricted oxygen, preferably 4 to 12% of ambient, and at temperatures of about 675-850 degrees F. As previously mentioned, although ambient air may be used as process gas, in accordance with the preferred embodiment of the present invention, the process gas is comprised of a high oxygen content gas, such as, but not limited to, raw oxygen. The use of such oxygen rich gases not only prevents the formation of regulated pollutants, such as nitrous oxides, but also allows for structural components, such as the at least one gasification chamber 12a, 12b, vents, and associated ducting, of the unit 10 to be smaller then would be required if an abundance of undesirable gases accompanied the desired oxygen.

[0095] As process temperatures and oxygen levels reach desired ranges, the gasification of the waste material commences. As previously mentioned, the combination of offsetting the mesh liner 58 and support rails 92 away from the adjacent walls 22a, 22b, 22c, 22d, 24,26 23a, 23b of the exterior vessel 30a, 30b and the gaps in the said liner 58 and rails 92 allow process gases to flow around, and into the top, bottom, and side surfaces of the loaded waste material. Exposing all sides of the loaded waste material to process gas increases the surface area of waste material that is exposed to process gas, and thus increases the size of the primary reaction zone. Because gasification cycle time is a function of surface area exposure to process gas, an increase in exposed surface area improves the

substochiometric combustion conditions that will produce produced fuel gas at a lower temperature. Furthermore, the decrease in required gasification temperatures assists in preventing reformation reactions similar to those that typically occur in mass bum incinerators.

[0096] In the accordance with the illustrated embodiment of the present invention that includes at least one maze ignition chamber 70a, the at least one produced gas igniter 78 is preferably activated prior to the gasification procedure to a temperature of approximately 1000 degrees F. Such early activation prevents the possibility that uncombusted gases may pass through the maze chamber 70a, thereby insuring the cleanliness of any emissions released to the atmosphere.

[0097] The gasification of the loaded waste material is a function of time, temperature, and oxygen concentration in the gasification chamber. Once the ambient temperature within the at least one gasification chamber 12a reaches approximately 350 degrees F. , the oxygen content in the at least one gasification chamber 12a will be significantly depleted. At this point, there will likely be a volume of produced gas hanging in the upper quarter of the at least one gasification chamber 12a, at which point the induced draft fan 102 may be turned on to withdraw or vent the produced fuel gases out of the at least one gasification chamber 12a and into the produced fuel gas combustion chamber 16a. The at least one gasification chamber 12a also preferably includes an oxygen sensor that indicates to the controller 98 whether the at least one process gas inlet 116 should be opened so as to allow additional process gas to enter into the at least one gasification chamber 12a.

[0098] The controller 98 preferably determines when to activate the induced draft fan 102 of the fuel extraction assembly 100. As previously mentioned, The fan 102 is preferably configured to create a pressure in the produced fuel gas combustion chamber 16 that assists in withdrawing produced fuel gases out of the gasification chamber 12a. The controller 98 also preferably determines when to send a signal to the motor 105 that controls the opening and closing of the gate valve 104, so that the process of removing produced fuel gases from the gasification chamber 12a may commence.

[0099] In accordance with the illustrated embodiment of the present invention in which the produced fuel gas combustion chamber 16 is a maze ignition chamber 70, a supplemental flare gas, preferably in the form of a high oxygen content gas or hydrogen gas, or some combination thereof, is added to the produced fuel gases in the inner chamber 74 of the maze 70 prior to combustion. However, as previously mentioned, the addition of supplemental flare gas to the produced fuel gas may occur prior to passage of the produced fuel gas into the produced fuel gas combustion chamber 16.

[00100] Produced fuel gases typically enters the produced fuel gas combustion chamber 16 at the same temperature as the gasification chamber 12a itself, i. e. approximately 800 degrees F. In the embodiment of the present invention in which the produced fuel gas combustion chamber 16 is a maze 70a, the combustion of the produced fuel gases by the at least one produced gas igniter 78 preferably raises the temperature of the inner chamber 74 to an approximate range of 1600 degrees F. The maintenance of an optimal 1,600 degrees F. for 2 seconds retention time or greater, is controlled by the size of the combustion maze and the interface of the process logic controller 98.

[00101] Following combustion of the gases, the gases flow through the winding passageway of the inner chamber 74 of the maze 70a, the winding passageway preferably being configured to create turbulence in the passing gases.

The winding pattern of the inner chamber 74 also increases the retention time of the gasses passing through the maze 70, thereby increasing the time the combusted gases are exposed to a hot environment. In the illustrated embodiment of the present invention, the retention time is approximately 2.7 seconds. The combusted gases then pass through the at least one exhaust port 88a, whereupon the hot air effluent is preferably directed into the enclosure of a primary end use device, such as, but not limited to, the base of a boiler so as to provide the energy for steam/hot water production in lieu of natural gas.

[00102] While the present invention has been illustrated in some detail according to the preferred embodiment shown in the foregoing drawings and descriptions, it will be understood that the invention is not limited thereto, since modifications may be made by those skilled in the art, particularly in light of the foregoing teaching. It is therefore contemplated by the appended claims to cover such modifications that incorporate those features that come within the spirit and scope of the invention.