Closed loop work station bioremediation using mini-reactor cartridges

Abstract

A system for capturing and neutralizing HAP's (hazardous air pollutants) and VOC's (volatile organic compounds) at the source point by providing a closed loop remediation system which utilizes an air collection, treatment and control module containing a predetermined size bay of multiple interchangeable mini-biofilter cartridges that function to consume the pollutant and recirculate remediated air back to the source point of the pollutant. The system includes establishing a closed loop air system at a work station which generates and emits VOC's, capturing the VOC's in the air stream flow and transporting them directly into an adjacent biofilter module which contains selected microorganisms in mini-cartridges or in a hopper which biodegrade said VOC's and recirculates remediated air back to the source point of the pollutant.

Description

BACKGROUND OF THE INVENTION

The present invention relates in general to a system for removal and treatment of pollutants in air, and more specifically to a source point closed loop remediation system. With respect to HAP (hazardous air pollutants) and VOC (volatile organic compounds) current methods of VOC removal include distillation; oxidation combustion ionization; biofiltration; and activated carbon adsorption. All of these methods are large whole-building fixed systems having high installation costs, and, with the exception of biofiltration, have high energy consumption and introduce new pollution considerations or generate hazardous waste.

The present invention includes the use of multiple small mini-reactor cartridges to reduce installation and repair or replacement and maintenance costs, permit incremental system expansion, and allow a variety of suitable mini-reactor based remediation technologies to be used together in series or parallel.

Present systems typically treat and exhaust an entire volume of building air without considering the actual pollution source and concentration, resulting in inefficient pollution removal. Furthermore, air heating or cooling of the makeup building air is required which adds to total energy consumed.

Biofiltration utilizes the natural process of biodegradation which in its most basic form occurs in a compost pile. Most typically, water-borne microbes consume the carbon in the organic matter of the pile, and release carbon dioxide and water. By passing an airstream containing an organic vapor (HAP/VOC) containing carbons through such a compost pile, the microbes will preferentially consume the more readily available carbon in the gas stream, thereby cleansing said airstream.

Notwithstanding initial installation costs, biofiltration is a proven and low energy cost, natural method of HAP/VOC remediation that has been in commercial use in large installations both in the United States and abroad for over 15 years. In biofiltration, no secondary carbon source (natural gas) is required to maintain combustion and make up for varying concentrations of VOC laden air as in the most widely employed oxidation process; and no hazardous waste is generated as with carbon absorption; and no by-products other than water and carbon dioxide are released. Distillation is usually not economically practical due to relatively low work place concentrations and value of the recovered chemical.

Because of their large size and method of construction and operation, current bioremediation systems have relatively high installation, secondary energy consumption and operational costs approaching the other methods.

Current biofiltration technology includes the use of naturally biodegradable media such as compost and vegetation as the supporting media and the source of both microbes and nutrients, and has proven to have inconsistent and relatively uncontrollable and repeatable long term field performance.

The present invention includes complete control of the microbial environment with the use of stable artificial media in conjunction with controlled water and nutrient addition for consistent operation. The present invention further includes the inoculation of said environment with specifically isolated and custom grown inoculate tailored to the VOC/HAP to be remediated to maintain high and consistent removal efficiency.

With respect to bioremediation, the following prior art is representative of the state of the art with respect to treating HAP's and VOC's.

U.S. Pat. No. 3,880,061 broadly relates to a contamination free work station by providing an air stream across the work station to remove any contaminants through filter means as shown in the figure.

U.S. Pat. No. 4,734,111 is directed to a process and apparatus for cleaning spent air or air polluted with styrene and filtering out the styrene in an apparatus and process which uses a specific biofilter utilizing a spruce bark and microorganisms thereon to degrade the styrene.

U.S. Pat. No. 5,409,834 relates to an invention and apparatus for removing pollutants from a source of polluted air such as a work paint station (see FIG. 1). Polluted air from the work station is introduced from a supply conduit into a wet plenum chamber which has a spray nozzle which sprays microbial laden liquid into the incoming polluted air.

U.S. Pat. No. 5,691,192 is related to a biological filter for removing volatile compounds from gas emissions such as styrene. The styrene is broken down with a fungus which is contained on a carrier or inert material such as perlite. Activated carbon may also be added to the mixture.

U.S. Pat. No. 5,869,323 is directed to a biofilter which uses a bioreactor treatment tank comprising at least one bioreactor bed and in which the air filtration is conducted such that the air flow through the tank is from the top downward, with the biofiltration being conducted under pressures of less than an ambient.

These inventions teach the conventional type of prior art systems which are used for aerobic bioremediation in commercial plants. All the above, and this patent pertain to aerobic biofiltration wherein the biodegradation occurs on the surface of a water film by a consortium of aerobic microbes.

U.S. Pat. No. 6,010,900 is directed to enhancing biodegradation using a bioreactor. The bioreactor contains an aqueous phase in which a microorganism capable of degrading a sparingly soluble volatile organic compound is contained. The patent further teaches contacting the solution with a gas/vapor stream comprising the sparingly soluble volatile organic compound such that the soluble volatile organic is solubilized in the aqueous phase to form an enriched solution, and then incubating the enriched solution so that the microorganism degrades the solubilized sparingly soluble volatile organic compound thereby enhancing biodegradation. (This is an anaerobic process and is not related to the present invention).

It can therefore be seen from the above cited commercial practices and prior art that there is a need for a bioremediation system which reduces natural gas and energy consumption and high fixed and operation costs of remediation; adds efficiency, control and repeatability to the bioremenation process; and does not produce hazardous waste by-products as is typical of the current prior art systems.

SUMMARY OF THE INVENTION

It is therefore an object of the present invention to provide a shipable by common carrier, expandable, movable, modular components, cartridges or hopper based closed loop system for remediation of HAP/VOC's within a manufacturing plant at the source.

It is another object of the present invention to provide an efficient biological system which reduces HAP/VOC's to water and carbon dioxide.

It is another object of the present invention to remediate process HAP/VOC's concentration over 90%.

It is yet another object of the present invention to provide a system for collection and neutralizing HAP's (hazardous air pollutants) and VOC's (volatile organic compounds) at the source point.

Another object is to contain the biological eco-system in multiple small biofilter cartridges or hoppers.

Another object is to use an artificial support media for the water film that supplies no naturally biodegradable matter and therefore will not degrade or compact.

Another object is to use natural media such as locally available compost.

Another object is the use of specifically isolated inoculate containing highly efficient microbe strain(s) tailored to maximally consume the VOC/HAP to be remediated.

Another object is to provide or replace appropriate nutrient addition to enhance microbial growth.

Another object is to provide and maintain a suitable water film to the media to sustain the inoculate eco-system.

Another object is to replenish the media water film and adjust it by periodically and discontinuously bio-recirculating inoculate and nutrient laden water through the media at a low flow rate.

Another object is to flush excess biomass and H₂S and cleanse and reactivate the media by periodically and discontinuously filtering and recirculating inoculate and nutrient laden water through the media at a high flow rate.

Another object is to collect, filter, store, neutralize, replenish and recirculate the nutrient and inoculate laden water within a remediation system at the work station.

Another object is to allow reversal of the airstream flow through reactor cartridges or hoppers.

Another object is to contain air and water functions in remediation modules.

Another object is to allow system reversal of the airstream direction through a cartridge or hopper.

Another object is to allow for series and/or parallel airflow through multiple cartridges or hoppers.

Another object is to allow various cartridges or hoppers to contain differing media, inoculate, and/or remediation methods.

Another object is to allow individual replacement of a single cartridge or hopper in a remediation system.

Another object is to use the reactor cartridge/hopper embodiment for other granular remediation techniques.

Another object is to include exhaust stream dehumidifcation.

Another object is to combine all remediation system functions in a single cartridge assembly or hopper module assembly.

The present invention is directed to providing a closed loop modular remediation system which includes air collection with air and water treatment and control and contains a predetermined size bay of multiple interchangeable cartridges or hoppers that function to consume the pollutant and recirculate remediated air back to the source point of the pollutant.

In one embodiment, a closed loop air stream is established at a work station area involving fiberglass laminating which generates and emits the styrene HAP, which is captured by the air stream flow which transports the emitted styrene directly into an adjacent biofilter module system as described above which contains selected microorganisms in multiple mini-biofilter cartridges which consume the styrene, and recirculates the remediated air back to the source point of the pollutant at the work station. The air flow is continuous and the system serves to maintain the styrene level at the work station at safe levels.

In a further embodiment, multiple sources of contaminants in a given room or area can be captured and treated at a single remediation station or multiple remediation stations can be used within a given room or area to treat higher concentrations.

A further embodiment includes the cleansing of methane containing deleterious H₂S by biodegrading the H₂S using biofilter cartridges or a larger reactor in the form of a hopper.

BRIEF DESCRIPTION OF THE DRAWINGS

For a further understanding of these and objects of the invention, reference will be made to the following detailed description of the invention which is to be read in connection with the accompanying drawing, wherein:

FIG. 1 is a front view with partial break away of a self-contained air collection, treatment and control module containing multiple biofilter cartridges used in the system of the present invention.

FIG. 2 is a schematic side view of a self-contained single cartridge remediating system for treating a small source.

FIG. 3 is a side elevational view of a second reactor cartridge used in the present invention having upward airflow.

FIG. 4 is a partial sectional view of the cartridge of FIG. 3 with the bottom of the cartridge disassembled.

FIG. 5 is a partial sectional view of the cartridge of FIG. 4 with the bottom assembled illustrating the down flow of the gas being treated opposite to FIG. 1.

FIG. 6 is a partial section view of the cartridge of FIG. 5 in which the inlet tube has been deleted.

FIG. 7 is a perspective view of a hopper module having removable hopper inserts.

FIG. 8 is a perspective view of a second embodiment of a hopper module having removable inserts.

FIG. 9 is a perspective view of the hopper insert of FIG. 7 illustrating the trap door feature of the hopper insert.

FIG. 10 is a partial sectional view through the top of the hopper module along line 10-10.

FIG. 11 is a side sectional view through the reservoir of the hopper module.

DETAILED DESCRIPTION OF THE INVENTION

The present invention is more fully understood with reference to the drawings where FIG. 1 illustrates a closed loop system 10 for treating a work station area or module 12 which collects and remediates a source of pollutant such as styrene generated from laminating with fiberglass. The module contains end walls, 11 and 13 and connecting side walls (not shown), upper manifold 15 and lower manifold 17 and a centrally located control console 19, also described as a control housing assembly, (not shown) which functions to control the timing and sequencing of the various pumps and blower which control the water and air flow of the system. This hardware and electronics control the operation of the system and are conventional in the art. The upper and lower manifolds provide a support means to hold a plurality of cartridges 14 in place and allow them to be easily removed for replacement or repair. The upper manifold is mounted to and supported by end walls 11 and 13 and control console 19. As illustrated in FIG. 1, compressible seal members 21 function to hold the cartridges in place, with the seal means functioning to seal the top and bottom of the cartridge which fits between the upper and lower manifold structure at 23 and 25. It should be understood that any conventional support and sealing means available in the art may be used to seal and hold the interchangeable cartridges in place. For example, springs, hinges, a snap-fit geometry or any combination thereof may be used to hold the cartridges in place. Any conventional sealing means, such as O rings, cushioning foam, interlocking contact surfaces and the like, any be used. The closed loop ducting system contains an array of interchangeable mini-biofilter cartridges 14 which contain a carrier medium 16 supporting a water film suitable for microorganisms or a mix of microorganisms on the carrier surface which have been selected to degrade the styrene or other VOC's of interest. The cartridge(s) is preferentially filled with a suitable inert carrier material such as perlite or an inert synthetic material such as plastic or a ceramic. A moisturized and nutrientized airflow through the biofilter promotes the growth of indigenous or synthesized microorganisms on the surface of the carrier material which through the action of the microorganisms acts to biodegrade the HAP and/or VOC's of interest. Suitable microorganisms which can be used to promote this degradation include bacteria, such as Pseudomonas and Mycobacterium. Other suitable natural occurring materials which contain indigenous microorganisms such as compost, peat, soil, wood chips, plant residues and tree bark may also be used or included. The reversible biofilters contain an outer housing or shell 15 suitability made of plastic and contain a perforated top and bottom, 18 and 20 respectively, which may include a screen to allow for air flow and water flow through the biofilter. Interconnecting ducting 22 passes a flow of contaminated air from the room through the bottom of the biofilters with remediated air passing back into the room through ducting 24. Pump 25 functions to recirculate and replenish the inoculated nutrient laden water film on the carrier material in the biofilters which enhances the action of the microorganisms in degrading the styrene. Pump 25 preferentially draws water from lower collection trough 28 which has received excess water from the biofilters 14. Pump 25 then recirculates the water to the top of the biofilter through water manifold 30 and nozzles 32. In FIG. 1, which is not drawn to scale, area or room 12 is depicted as grossly smaller in size than the closed loop system 10. For example the cartridges 14 are typically about 30 inches in height and 15 inches×15 inches in cross-section. The discrepancy in relative sizes is to better show the detail of the closed loop system.

Although in FIG. 1 where multiple cartridges have been used to illustrate the invention, it should be understood that larger reactors in the form of a hopper and or hopper module may be used where larger amounts of media are required. Generally, the hopper handles significantly larger amounts of carrier or media and the hopper inserts are moved in and out of position by mechanical means.

In a further embodiment of the present invention as shown in FIG. 2, a single independent mini-reactor cartridge 40 is illustrated. The cartridge contains an outer housing 42 and is open at both ends 44 and 46 with supporting grilles (not shown) to contain the carrier media. The cartridge contains an upper clip-on blower housing 48 which contains an exhaust fan 50 and an exhaust port 52. The blower housing is attached to the cartridge by latch 54 and ring seal 56. A water reservoir 58 is attached to the bottom of cartridge 40 by latch 60 and ring seal 62. The reservoir contains water 64 and optionally a wicking humidifier filter 66. In operation, air to be treated is drawn in through inlet 68 and humidified in reservoir 58. A suitable source of microorganisms contained on a carrier media 70 in the housing degrade the VOC of interest as previously described herein. The arrows in the drawing depict the flow path with the remediated air passing through media 70 and exiting through exhaust port 52.

A water recirculation pump 72 and associated water transfer manifold 74 may optionally be added to recirculate the microbe and nutrient laden water from the reservoir 58 to the top of the reactor cartridge 40. Optionally dehumidification may be required to lower exit air moisture buildup.

A single cartridge system of the type shown in FIG. 2 was used for evaluation and testing. The mini-reactor cartridge measured 15″ square and 30″ tall with 8-½″ square inlet and outlet grilled openings at opposite ends. The nominal inside volume of the cartridge was approximately 3.6 cubic feet. The cartridge with a bottom grille installed, weighs approximately 16 pounds. The reactor was then loaded with 30 pounds of coarse perlite media, for a total cartridge plus media dry weight of about 46 pounds.

The blower housing as shown in FIG. 2 was attached to the top of the cartridge along with a water replenishment port and water recirculating hose, and a small water recirculating submergible pump was installed in the water reservoir. The system was assembled by placing the cartridge on top of the water reservoir and then adding the blower housing on top of the cartridge to make up a basic system as described in FIG. 2.

The system parameters were then adjusted to achieve a 5 CFM airflow giving a nominal 45 second empty bed dwell time. The water flow was set at a nominal flow of 8 oz./hr. to supply sufficient bed moisture in the range of 4 oz./hr. to account for evaporation due to a 40% RH ambient air, plus an additional 100% excess to maintain some trickling flow through the bed.

The system was then loaded with 2 gallons of inoculate and nutrient mixed in water. The inoculate used was Pseudomonas Putida which is capable of growth on toluene and is grown on a dilute minimal medium using styrene as a sole carbon and energy source. The inoculate is used in a concentration of about 10⁸ CFU/ml and introduced to the cartridge by trickling over the perlite. The nutrient used was a common slow release granular garden fertilizer sold by Agway under the trade name Osomocote.

A standard styrene source which releases 100 PPM styrene at 5 CFM was connected to the inlet port, and the system blower and pump were started up. Measurements were taken with a photo-ionization detector (PID) at the inlet and outlet of the system. Within 1 hour of startup, the average concentration in the outlet stream was 18 PPM, and after 24 hours had dropped under 9 PPM for a 90%+reduction in styrene concentration.

Earlier lab tests made on a similar size configuration set to the same airflow dwell time parameters, but using a horizontal lab reactor loaded with oak chips and natural compost, and with no water trickling or inoculate addition achieved a 75% removal rate after 7 days of operation, and maintained in that range for over 2 months until the test was terminated due to the bed drying out.

Another lab test using the same lab reactor and test setup and loaded with oak chips, and the inoculate, had faster startup results on the order of 4 days and better long term remediation on the order of 85%, until the natural bed settled and bed channeling occurred some time after 3 months. This was indicated by a decrease in remediation down to 80%. Disassembly of the reactor confirmed the channeling along with some bed dryup and compaction.

A further lab test using the same lab and test setup was loaded with plastic pellets and a water pump added to recirculate the water from the bottom of the reactor to the top. The Pseudomonas Putida inoculate described above was used with the addition of a slow release nutrient. Initial startup time was on the order of 2 days to reach a 80% removal rate, with 90% being reached after 4 days. The reactor efficiency continued to increase. Pump failure eventually occurred after another 10 days at which point the removal rate was up to 94%.

In a further embodiment of the present invention, the above described system may also be used for removing H₂S from methane (CH₄) or other suitable gaseous fuel which includes providing at least one biofilter cartridge which sustains microbial activity that will function to consume H₂S contained in a stream of methane gas. In this embodiment, a stream of methane gas which contains H₂S is transported directly into the biofilter system which contains at least one cartridge containing selected microorganisms which function to biodegrade H₂S. The clean methane gas is then recirculated to a source of use.

A suitable reactor cartridge which can be used for this embodiment includes an outer housing having a pair of oppositely disposed open ends. The housing which contains an inlet fan and an inlet port connected to a vertical inlet tube positioned at one end which also contains a water inlet and a gas outlet. A water reservoir is attached to the opposite end of the housing, with the reservoir further containing an outlet for the removal of water. In operation, a source of methane which contains H₂S to be treated is passed through the inlet and down the vertical tube and reverses direction at the bottom to go up through a suitable source of microorganisms contained in said housing which are selected to degrade the H₂S.

Aerobic microorganisms are used to remove the hydrogen sulfide from the gas stream and oxidize it back to sulfate, which then combines with water to form sulfuric acid. Initial testing indicated that cow manure compost, which contains sulfur oxidizing bacteria, can remove hydrogens sulfide (H₂S) from a gas stream with removal efficiencies above 80%.

Farm digester gas is not the only source of sulfide contaminated methane rich gas for which biofilteration technology may be suitable. Wastewater treatment plants, landfills, paper mills, and food processing plants are all capable of producing biogas. Additionally, as higher quality natural gas wells are depleted, it may become economical to exploit smaller, remote, sulfur contaminated wells, biofilteration with its modular nature and low operating costs may be the ideal technology for sulfur removal from these gas source.

One embodiment exemplary of the invention is illustrated in FIGS. 3-5 is directed to a system for removing hydrogen sulfide (H₂S) from methane (CH₄) or other suitable gaseous fuel. As shown in FIGS. 3-5 at least one biofilter cartridge 10 which sustains microbial activity can be used to consume H₂S contained in a stream of methane gas 19 that is introduced to the microorganisms at the top (FIG. 4) or bottom (FIG. 5) of the carrier media 11. As shown by the arrows in the drawings, a stream of methane gas 19 which contains H₂S is transported directly into a biofilter system which contains at least one cartridge containing selected microorganisms which function to biodegrade H₂S. The clean methane gas 26 is then recirculated to a source of use.

Carrier 11 may comprise any natural, artificial or synthetic such as compost, granular inert plastics, ceramics or crystalline materials which support and act as a carrier for the microorganisms or bacteria. Pearlite functions as an economical and readily available carrier or media. Any suitable microorganism or bacteria which functions to remove or biodegrade H₂S can be used. Suitable microorganism include Thiobacillus and Ralstonia. If a natural occurring or biodegradable material is used in place of a synthetic carrier, such as cow manure compost, tree bark or vegetation, then microorganisms indigenous to these materials will function to biodegrade the H₂S.

In FIG. 4, a suitable reactor cartridge 10 which can be used in the present invention includes an outer housing 12 having a pair of oppositely disposed open ends which are closed by a bottom support member 14 and a top support member 16. The housing contains an inlet fan or blower 18 and an inlet port 20 connected to a vertical inlet tube 22 positioned at one end which also contains a flush water inlet 24 and a gas outlet 29. A water reservoir 28 is contained in bottom member 14 at the opposite end of the housing, with the reservoir further containing an outlet 30 for the removal of flush water. In operation, a source of methane 19 which contains H₂S to be treated is passed through the inlet and down the vertical tube 22 and reverses direction at the bottom to go up through a suitable source of microorganisms contained in said housing which are selected to degrade the H₂S. The treated methane 26 is released through said gas outlet 29, at the top of the housing and captured for storage or direct use. The remote cartridge is also flushed by the down flow of water 25.

Support member 14 and 16 function to support and hold a given cartridge in place and allow for the cartridge to be readily removed and a new cartridge inserted in its place. It can be seen that the system allows for a self contained, removable cartridge(s) which provide for overall flexibility and efficiency.

FIG. 5 illustrates the same structure as FIG. 4 in which the methane 19 to be treated is forced by blower 18 through carrier 11 and upwardly through tube 27 through outlet 31. The water push 25 is employed as in FIG. 4.

The positioning, holding and sealing means described above with respect to FIG. 1 are readily adapted to the cartridges of this embodiment with respect to their removal and replacement.

FIG. 6 schematically illustrates an alternative embodiment of the present invention in which inlet tube 27 has been removed, and the methane flow 19 is from the bottom upward through carrier 11.

It should be understood that the present invention is not to be limited by the preferred embodiments of the mini-cartridge, which may be increased in size up to a maximum weight and volume that can be put on a pallet, moved by a factory pallet jack or fork lift, and shipped by common carrier. This is as opposed to current large permanent single reactor designs requiring a pit or rigging to install.

FIG. 7 illustrates a further embodiment of the present invention in which the above described cartridges (FIGS. 3-6) can be replaced with a hopper module 120 having removable hopper inserts 122 and 124. The hopper module and hopper inserts are the functional equivalent of the previously described cartridges and include side walls 126 and 128, a back wall 130 and optional front wall 132 and a movable or hinged top 134. The hopper module is sized to accommodate multiple (two or more) hopper inserts 122 and 124. The hopper inserts contain the same type of fill (media and microorganisms) as the cartridges, and are removably positioned between an upper and lower manifold or equivalent structure and function to clean methane gas as previously described above.

In the embodiment shown, a water reservoir 140 receives water from the top 134 of the hopper module through holes 136 of manifold 148, with the water trickling downwardly through the carrier or compost (not shown) contained in hopper inserts 122 and 124. The methane gas enters the module through inlet 144 (FIGS. 9 and 11) and passes upwardly through opening 154, and through the carrier, with the treated methane gas passing through outlet 146. Any suitable conventional blowers and pumps, such as previously described herein, are used to move the methane and water through the system.

The positioning, holding and sealing means described above with respect to FIG. 1 are readily adapted to the hopper module and hopper inserts described in this embodiment.

The hopper inserts are conveniently made in larger sizes than the cartridges to accommodate a greater mass of media material, such as cow manure compost, and are designed to be removed upwardly (FIG. 8) using screw eyes 150 or sideways using side flanges 152 (FIG. 9). The hopper concept is desired to be used in an agricultural or similar setting in which hoppers of a large size could be mechanically moved such as with farm equipment. A bottom trap door 138 allows for easy clean up or recharging of media.

While the present invention has been particularly shown and described with reference to the preferred mode as illustrated in the drawing, it will be understood by one skilled in the art that various changes in detail and configuration may be effected therein without departing from the spirit and scope of the invention as defined by the claims.

Claims

1. A system for removing H2S from methane (CH4) which includes providing at least one removable biofilter cartridge that functions to sustain microbial activity that will function to consume H2S contained in a stream of methane gas which comprises establishing a stream of methane gas which contains H2S and transporting said methane gas stream into a biofilter system which includes at least one cartridge containing selected microorganisms which function to biodegrade H2S, and recirculating clean methane gas to a source of use; wherein said cartridge comprises an outer housing having a pair of oppositely disposed open ends, said cartridge being further positioned by insertion between a closure member which contains an exhaust port positioned at one end of said housing and a second closure member in the form of a water reservoir positioned at said opposite end of said housing with said system further containing an inlet port for a source of gas to be treated, with said inlet and said exhaust ports being connected to a ducting system, and circulation means positioned to promote the flow of methane gas through said system, and where when a given cartridge is spent or damaged from use, it may be readily removed from the system and a new cartridge inserted in its place.

2. The system of claim 1 in which the cartridge is positioned vertically and water is circulated through the microorganisms.

3. The system of claim 1 where water is periodically flushed through the microorganisms at a fast rate.

4. The system of claim 1 where said water is filtered, pH neutralized, and optionally recirculated.

5. The system of claim 1 where said water is filtered and neutralized (pH).

6. The system of claim 1 in which the microorganisms are at least one isolated from the group consisting of bacteria.

7. The system of claim 1 in which the cartridges are positioned vertically and water is continuously trickled through the microorganisms.

8. The system of claim 2 in which the microorganism laden water film is supported on a carrier material.

9. The system of claim 7 in which the carrier is at least one artificial material selected from the group consisting of granular inert plastics.

10. The system of claim 7 in which the carrier is at least one artificial material selected from the group consisting of granular materials.

11. The system of claim 7 in which the carrier is at least one material selected from the group consisting of crystalline minerals.

12. The system of claim 7 in which the carrier or media consists of pearlite.

13. The system of claim 7 in which the carrier may include at least one natural material selected from a group consisting of biodegradable media such as compost, tree bark and vegetation.

14. A system for removing H2S from methane generated by animal waste which comprises: (a) providing a source which generates a biogas which contains a major portion of methane containing a relatively small amount of hydrogen sulfide (H2S); (b) providing a hopper module having an outer housing which contains a gas inlet, water inlet and gas outlet, and at least one removable hopper insert, a source of microorganisms contained within said module which are selected to degrade H2S; (c) passing a stream of said methane containing said H2S through said gas inlet and through said microorganism contained in said module whereby said H2S is degraded; (d) introducing a downward flow of flushable water, and (e) passing said treated methane through said gas outlet for storage or to a source of use.

15. The system of claim 14 in which at least one removeable hopper insert holds a carrier which contains said source of microorganisms.

16. The system of claim 15 in which the hopper module and hopper inserts are substantially rectangular in shape.

17. The system of claim 14 in which said hopper insert contains at least one moveable wall section which facilitates the cleaning of said hopper insert.

18. A hopper module which comprises an outer housing which receives and holds in place at least one removable hopper insert which includes a carrier material which contains a source of microorganisms which are suitable for degrading a biogas, said module further containing means for directing a source of biogas to be treated through said microorganism containing media, said hopper insert further containing means thereon for mechanically moving said module insert into and out of position in said module.

19. The module of claim 18 in which said module contains a lower water reservoir and an upper gas outlet and water inlet.

20. The module of claim 18 in which the hopper module and hopper insert are generally rectangular in shape.

21. The module of claim 18 in which the mechanical means for moving include at least one of side flanges and screw eyes.

22. The module of claim 18 which includes positioning and sealing means for said hopper inserts which allow said inserts to be easily removed and/or replaced.