WO1998009559A1 - Organic waste combustor - Google Patents
Organic waste combustor Download PDFInfo
- Publication number
- WO1998009559A1 WO1998009559A1 PCT/US1997/016659 US9716659W WO9809559A1 WO 1998009559 A1 WO1998009559 A1 WO 1998009559A1 US 9716659 W US9716659 W US 9716659W WO 9809559 A1 WO9809559 A1 WO 9809559A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- chamber
- further including
- waste
- organic waste
- cyclone burner
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
- F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/24—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a vertical, substantially cylindrical, combustion chamber
- F23G5/245—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a vertical, substantially cylindrical, combustion chamber with perforated bottom or grate
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/50—Control or safety arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N5/00—Systems for controlling combustion
- F23N5/003—Systems for controlling combustion using detectors sensitive to combustion gas properties
- F23N5/006—Systems for controlling combustion using detectors sensitive to combustion gas properties the detector being sensitive to oxygen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/40—Gasification
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/10—Combustion in two or more stages
- F23G2202/101—Combustion in two or more stages with controlled oxidant supply
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/10—Combustion in two or more stages
- F23G2202/102—Combustion in two or more stages with supplementary heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/30—Cyclonic combustion furnace
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/40—Stationary bed furnace
- F23G2203/403—Stationary bed furnace with substantial cylindrical combustion chamber
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2204/00—Supplementary heating arrangements
- F23G2204/10—Supplementary heating arrangements using auxiliary fuel
- F23G2204/101—Supplementary heating arrangements using auxiliary fuel solid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2207/00—Control
- F23G2207/10—Arrangement of sensing devices
- F23G2207/101—Arrangement of sensing devices for temperature
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2207/00—Control
- F23G2207/30—Oxidant supply
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2207/00—Control
- F23G2207/40—Supplementary heat supply
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2237/00—Controlling
- F23N2237/16—Controlling secondary air
Definitions
- This invention relates to waste disposal through complete organic combustion by a process known as Pyrolysis.
- Waste streams range from relatively benign materials such as raw wood chips, used office paper, and fresh grass clippings, to hazardous materials such as biologically contaminated materials, fuel contaminated soil and pesticide tainted vegetation .
- Benign waste streams are typically landfilled at local municipalities. Unfortunately, the sheer volume of waste processed in this manner usually renders the landfill unsuitable for further commercial use. Hazardous waste streams that ar landfilled dramatically increase risk to the environment by leaching into water supplies and emitting harmful volatile components into the atmosphere.
- Incineration has the advantage of reducing the volume of waste into a landfill by as much as 97% and can render biological and chemical waste streams harmless.
- incineration can also release unacceptable levels of pollution into the atmosphere so incineration reactors must be fitted with expensive and complex post combustion controls to reduce hazardous emissions.
- the present invention uses a dual chamber combustion system. Reference herein is made to figures 1,2, 3, 4, 5, 6, 7A, and 7B. Overvi ew
- waste is decomposed by heat (Pyrolysis) in an oxygen starved environment.
- This partial combustion generates combustible particulates and flammable gases (lean gas) leaving only a small amount of sterile and generally inorganic ash.
- the lean gas is ducted (13) into a second chamber (cyclone oxidizer) (14) where it is mixed with sufficient oxygen and is completely combusted at high temperature.
- the resulting effluent is only minimally polluting.
- Waste is introduced into the machine through a pneumatically activated sliding charging portal drawer (10) .
- the drawer (10) has no sliding seals which require precision machining and are prone to mechanical failure. Seal integrity is critical since the pyrolytic process requires precision control of air flow.
- the drawer (10) In order to allow for continuous feeding for maximum throughput, the drawer (10) must be double sealed or the process will be disrupted and toxic fumes may leak into the immediate environment. .An automated air purging system in the drawer compartment provides an additional level of safety for operators of the equipment .
- the size of the drawer (10) is large enough to handle most bagged waste so shredding is not necessary, further reducing the risk to the operator.
- the machine After a bag of waste has been loaded (21) into the drawer (10), the machine is sealed (22A-22B) and the drawer delivers the waste (30) into the gas generator (11) .
- the drawer (10) has sensors to determine its position. When the drawer has returned to its original position (figure 2), it is ready to receive another charge of waste.
- waste Once the waste has entered the gas generator (16), combustion begins.
- the waste is maintained in a vertical column supported by a heat resistant grate (12) .
- New waste travels down the column as older waste is consumed in the generator. This process is defined by increasing temperature zones ranging from 100 C at the top to 1000 C at the grate (12) .
- Zone 1 Drying and Degassing: Water and light volatiles are vaporized.
- Zone 2 Gasification: Solid material begins to gasify under oxygen poor conditions.
- Zone 3 Coke Bed: Ungasified materials (mostly carbon) form a high temperature bed of coals .
- the formation of the coke bed and the production of gas is initiated by a grid of electric heating elements located at the grate (12). Once the process has reached an optimum temperature, the elements are shut off and the process continues unassisted. If the process drops below optimum temperatures, the heating elements are automatically restarted. This is necessary only when the waste stream is laden with non-combustible liquid.
- the grate (12) is a heat resistant rod design that allows ash to fall through into a containment compartment (15) .
- the design of the grate (12) allows for passive control of the size and amount of ash that passes into the compartment (15).
- a comb of stainless steel fingers (60) is selectively rotated between the rods to clear blockage and to agitate the column of decomposing waste to allow it to settle properly.
- Clean-out ports are located above the grate (12) to facilitate the removal of large inorganic objects that may collect on grate 12.
- the gas generator should be completely cool before this port may be opened. Normal operation renders all the carbon to ash.
- the grate (12) may be changed to allow more waste to be processed with an accompanying increase in the volume of ash .
- the ash compartment (15) is accessible through a clean- out port.
- the gas generator (16) should be completely cool before this port is opened.
- Lean gas produced from the waste is forced to pass through the coke bed in order to leave the gas generator (16) .
- the carbon and the heat react with the lean gas to breakdown or "crack" long-chain hydrocarbons which are the source of extremely hazardous emissions.
- the cracked gas is ducted to the cyclone oxidizer (14) through a circular transfer tube (13) .
- Regulated air secondary air
- the mixture spontaneously ignites in the oxygen rich environment and enters the pre-heated cyclone oxidizer (14) .
- the mixture remains in the cyclone oxidizer (14) under extremely turbulent conditions until it is completely oxidized rendering it harmless.
- the cyclone oxidizer (14) preferably has an octagonal cross section.
- the shape maintains the mixing efficiency of more traditional circular designs but is easier to construct and insulate.
- the dimensions of the oxidizer are calculated to insure maximum efficiency based on the volume of gas produced given the capacity of the gas generator .
- Auxiliary fuel is added to the axial tube (13) for preheating the cyclone oxidizer and for maintaining the proper temperature in the oxidizer (14) .
- the temperature may fall for two reasons: a) the heat content of the waste stream is too low, and b) the amount of lean gas produced during start up and shut down is too low. Both conditions require that auxiliary fuel be added to sustain the process to keep emissions within acceptable limits.
- the transfer tube (13) contains a grid of electric heaters.
- the grid has the additional benefit of dramatically reducing emissions on start-up.
- the primary method of control is through temperature feedback (figure 7A) . Probes are positioned throughout the machine to provide input for computer control. Secondary control is provided by oxygen and carbon monoxide sensors at the e.xhaust port ( Figure 7B) .
- the temperature in the cyclone oxidizer (14) is controlled by the amount of lean gas and secondary air that is mixed in the transfer tube (13) .
- the amount of lean gas is controlled by the amount of heat produced in the gas generator (16) .
- the amount of heat produced in the gas generator (16) is controlled by the amount of primary air that is injected into it.
- the computer uses the temperature and emission data to meter the primary and secondary air flow and to add auxiliary fuel or electric heat to the system.
- the computer displays continuous numeric and graphic readouts of all the parameters that it monitors and controls.
- the goals of the computer control is to reduce harmful emissions and to maximize throughput of the machine.
- Harmful emissions are reduced through temperature control .
- Throughput is maximized by water injection.
- the capacity of the gas generator is not volume dependent, rather, it is heat capacity dependent .
- waste high in heat capacity is added to the system, water is injected to absorb some of the heat content. This has the effect of raising throughput.
- the exhaust that leaves the system is hot, non- hazardous, and energy laden.
- the energy can be recovered by a boiler, heat exchanger, or heat pump. Heat recovery may be added to the transfer tube to eliminate the need for water injection.
- the present invention provides a means for safe, reliable, and economical disposal of organic waste. It features volume reduction, complete destruction, and minimal handling of waste streams. In addition, it is less expensive to maintain, simpler to operate, easier to adapt to existing systems due to its modular design, and more thermally efficient than current designs.
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU44262/97A AU4426297A (en) | 1996-09-05 | 1997-09-04 | Organic waste combustor |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US2468896P | 1996-09-05 | 1996-09-05 | |
US60/024,688 | 1996-09-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998009559A1 true WO1998009559A1 (en) | 1998-03-12 |
Family
ID=21821881
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1997/016659 WO1998009559A1 (en) | 1996-09-05 | 1997-09-04 | Organic waste combustor |
Country Status (2)
Country | Link |
---|---|
AU (1) | AU4426297A (en) |
WO (1) | WO1998009559A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102006013403B4 (en) * | 2006-03-23 | 2008-08-14 | Seemann, Uwe, Dipl.-Ing. | Method and device for exhaust air purification |
CN106439845A (en) * | 2016-11-18 | 2017-02-22 | 无锡大功机械制造有限公司 | Garbage drying head |
Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3785305A (en) * | 1972-05-03 | 1974-01-15 | Aqua Chem Inc | Incinerator |
US3855950A (en) * | 1973-10-10 | 1974-12-24 | Consumat Syst Inc | Automatic loading and ash removal system for incinerators |
US3861335A (en) * | 1973-08-20 | 1975-01-21 | Progressive Trade Corp | Incineration system |
US3880098A (en) * | 1974-03-25 | 1975-04-29 | Environmental Control Products | Metering apparatus for incinerator ash pit |
US4038032A (en) * | 1975-12-15 | 1977-07-26 | Uop Inc. | Method and means for controlling the incineration of waste |
US4261267A (en) * | 1979-03-23 | 1981-04-14 | Lesmeister Adrian Z | Furnace door |
GB2196099A (en) * | 1986-10-11 | 1988-04-20 | Erithglen Ltd | Furnace |
US4934283A (en) * | 1989-09-08 | 1990-06-19 | Partnerships Limited, Inc. | Solid waste disposal unit |
US5178076A (en) * | 1991-09-06 | 1993-01-12 | Hand David J | Bio-mass burner construction |
US5261335A (en) * | 1992-12-29 | 1993-11-16 | Blevins Jr Leslie | Firebox furnace with automatic feeding system |
US5279234A (en) * | 1992-10-05 | 1994-01-18 | Chiptec Wood Energy Systems | Controlled clean-emission biomass gasification heating system/method |
US5391074A (en) * | 1994-01-31 | 1995-02-21 | Meeker; John | Atmospheric gas burner and control system |
US5520123A (en) * | 1995-01-30 | 1996-05-28 | The United States Of America As Represented By The Administrator Of The Environmental Protection Agency | Intelligent afterburner injection control to minimize pollutant emissions |
US5678494A (en) * | 1995-03-22 | 1997-10-21 | Ulrich; Gael | Biomass-fueled furnace |
US5680821A (en) * | 1994-02-04 | 1997-10-28 | Advanced Envirotech Systems, Inc. | Solid waste handling and conveying apparatus |
-
1997
- 1997-09-04 WO PCT/US1997/016659 patent/WO1998009559A1/en active Application Filing
- 1997-09-04 AU AU44262/97A patent/AU4426297A/en not_active Abandoned
Patent Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3785305A (en) * | 1972-05-03 | 1974-01-15 | Aqua Chem Inc | Incinerator |
US3861335A (en) * | 1973-08-20 | 1975-01-21 | Progressive Trade Corp | Incineration system |
US3855950A (en) * | 1973-10-10 | 1974-12-24 | Consumat Syst Inc | Automatic loading and ash removal system for incinerators |
US3880098A (en) * | 1974-03-25 | 1975-04-29 | Environmental Control Products | Metering apparatus for incinerator ash pit |
US4038032A (en) * | 1975-12-15 | 1977-07-26 | Uop Inc. | Method and means for controlling the incineration of waste |
US4261267A (en) * | 1979-03-23 | 1981-04-14 | Lesmeister Adrian Z | Furnace door |
GB2196099A (en) * | 1986-10-11 | 1988-04-20 | Erithglen Ltd | Furnace |
US4934283A (en) * | 1989-09-08 | 1990-06-19 | Partnerships Limited, Inc. | Solid waste disposal unit |
US5178076A (en) * | 1991-09-06 | 1993-01-12 | Hand David J | Bio-mass burner construction |
US5279234A (en) * | 1992-10-05 | 1994-01-18 | Chiptec Wood Energy Systems | Controlled clean-emission biomass gasification heating system/method |
US5261335A (en) * | 1992-12-29 | 1993-11-16 | Blevins Jr Leslie | Firebox furnace with automatic feeding system |
US5391074A (en) * | 1994-01-31 | 1995-02-21 | Meeker; John | Atmospheric gas burner and control system |
US5680821A (en) * | 1994-02-04 | 1997-10-28 | Advanced Envirotech Systems, Inc. | Solid waste handling and conveying apparatus |
US5520123A (en) * | 1995-01-30 | 1996-05-28 | The United States Of America As Represented By The Administrator Of The Environmental Protection Agency | Intelligent afterburner injection control to minimize pollutant emissions |
US5678494A (en) * | 1995-03-22 | 1997-10-21 | Ulrich; Gael | Biomass-fueled furnace |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102006013403B4 (en) * | 2006-03-23 | 2008-08-14 | Seemann, Uwe, Dipl.-Ing. | Method and device for exhaust air purification |
CN106439845A (en) * | 2016-11-18 | 2017-02-22 | 无锡大功机械制造有限公司 | Garbage drying head |
Also Published As
Publication number | Publication date |
---|---|
AU4426297A (en) | 1998-03-26 |
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