EP1736527A1 - Method and device for feeding inflammables to gasifying furnace, and gasification melting system - Google Patents
Method and device for feeding inflammables to gasifying furnace, and gasification melting system Download PDFInfo
- Publication number
- EP1736527A1 EP1736527A1 EP03706956A EP03706956A EP1736527A1 EP 1736527 A1 EP1736527 A1 EP 1736527A1 EP 03706956 A EP03706956 A EP 03706956A EP 03706956 A EP03706956 A EP 03706956A EP 1736527 A1 EP1736527 A1 EP 1736527A1
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- EP
- European Patent Office
- Prior art keywords
- combustibles
- supplying
- combustible
- gasification furnace
- hopper
- Prior art date
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- 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
- F23G5/30—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a fluidised bed
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/50—Fuel charging devices
- C10J3/503—Fuel charging devices for gasifiers with stationary fluidised bed
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/723—Controlling or regulating the gasification process
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- 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
- F23G5/006—General arrangement of incineration plant, e.g. flow sheets
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- 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
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- 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
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
- C10J2200/154—Pushing devices, e.g. pistons
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
- C10J2200/156—Sluices, e.g. mechanical sluices for preventing escape of gas through the feed inlet
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
- C10J2200/158—Screws
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1625—Integration of gasification processes with another plant or parts within the plant with solids treatment
- C10J2300/1628—Ash post-treatment
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1625—Integration of gasification processes with another plant or parts within the plant with solids treatment
- C10J2300/1637—Char combustion
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1693—Integration of gasification processes with another plant or parts within the plant with storage facilities for intermediate, feed and/or product
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/303—Burning pyrogases
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- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/20—Combustion to temperatures melting waste
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/30—Combustion in a pressurised chamber
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/10—Waste feed arrangements using ram or pusher
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/12—Waste feed arrangements using conveyors
- F23G2205/121—Screw conveyor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/14—Waste feed arrangements using hopper or bin
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/16—Waste feed arrangements using chute
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/18—Waste feed arrangements using airlock systems
Definitions
- the present invention relates to a method and apparatus for supplying combustibles, such as municipal wastes, industrial wastes, biomass wastes, medical wastes, or automobile wastes including tire wastes, shredder dust, and the like, to a gasification furnace which gasifies the combustibles into a combustible gas, and to a gasification and slagging combustion system.
- combustibles such as municipal wastes, industrial wastes, biomass wastes, medical wastes, or automobile wastes including tire wastes, shredder dust, and the like
- FIG 1 is a diagram showing a schematic arrangement example of a fluidized-bed gasification furnace and a combustible supplying apparatus for supplying combustibles into the fluidized-bed gasification furnace which are used in this type of gasification and slagging combustion facility.
- the fluidized-bed gasification furnace 10 holds a fluidized medium at a lower portion thereof, and a fluidized bed 11 of the fluidized medium is formed by supplying a fluidizing gas 12 from a lower portion of the furnace.
- Combustibles 14 introduced through a combustible introduction port 13 are gasified by partial combustion under a reducing atmosphere in the fluidized bed 11.
- This type of fluidized-bed gasification furnace 10 is generally operated so that the pressure in the furnace is a negative pressure of about -50 mm Aq. Accordingly, a large amount of external air which has not been preheated leaks through the combustible introduction port 13 into the furnace. The leaked air which has not been preheated is consumed by combustion at the freeboard 15 in the fluidized-bed gasification furnace 10. The combustible gas combusted in part by the leaked air is introduced through the combustible gas outlet port 16 into the slagging combustion furnace. Combustion air to be supplied to the slagging combustion furnace is generally preheated so as to increase the temperature of the slagging combustion furnace.
- dampers having a sealing function are doubly provided in a chute connected to the combustible introduction port 13 (which corresponds to a portion between a combustible supplying means 30 and a combustible supplying means 33 connected to an upper stage of the combustible supplying means 30 in FIG 1) and combustibles 14 introduced into a hopper 38 by a crane 21 are supplied through the double damper 19 into the combustible supplying means 30 by a screw 34 while external air is prevented from entering the fluidized-bed gasification furnace 10 through the combustible introduction port 13 by sealing effects of the double damper 19.
- double damper dampers having a sealing function
- the hopper 38 is intermittently supplied with combustibles 14, the amount of combustibles 14 stored in the hopper 38 has large variations. Furthermore, combustibles 14 themselves have variations in quality. Therefore, fixed quantity supply cannot necessarily be achieved by the screw 34.
- the present invention has been made in view of the above drawbacks, and it is, therefore, an object of the present invention to provide a method and apparatus for supplying combustibles to a gasification furnace and to a gasification and slagging combustion system which can prevent leakage of external air into the gasification furnace, reduce a variation of a produced gas, and facilitate operational control for stable gasification.
- a method of supplying combustibles to a gasification furnace for gasifying the combustibles is characterized by comprising supplying the combustibles to a hopper while preventing external air from leaking into the gasification furnace by the combustibles themselves, and supplying the combustibles in the hopper to the gasification furnace in fixed quantity while controlling an amount of combustibles stored in the hopper so as to be constant.
- combustibles are supplied to a hopper while external air is prevented from leaking into the gasification furnace together with the combustibles by the combustibles.
- the combustibles in the hopper are supplied to the gasification furnace in fixed quantity while an amount of combustibles stored in the hopper is controlled so as to be constant. Accordingly, it is possible to reduce a variation of a combustible gas produced in the gasification furnace and facilitate stable operation of the gasification furnace. Further, since a variation of a combustible gas produced is thus reduced, it is also possible to facilitate stable operation of a slagging combustion furnace subsequent to the gasification furnace.
- a method characterized in that a combustible gas which leaks from the gasification furnace to a combustible supplying side is released to a waste pit.
- a combustible gas which leaks from the gasification furnace to a combustible supplying side can be treated safely by releasing the combustible gas to a waste pit because air is continuously drawn from the waste pit for deodorization and used for combustion.
- a combustible supplying apparatus for supplying combustibles to a gasification furnace for gasifying the combustibles
- the combustible supplying apparatus is characterized by comprising a first combustible supplying mechanism for supplying the combustibles while preventing external air from leaking into the gasification furnace, a hopper for storing the combustibles supplied through the first combustible supplying mechanism, and a second combustible supplying mechanism for supplying the combustibles in the hopper to the gasification furnace in fixed quantity while controlling an amount of combustibles stored in the hopper so as to be constant.
- combustibles are supplied to a hopper by the first combustible supplying mechanism while external air is prevented from leaking into the gasification furnace.
- external air can be prevented from leaking into the gasification furnace, and it is not necessary to provide any special sealing mechanisms such as a double damper.
- the combustibles in the hopper are supplied to the gasification furnace in fixed quantity by the second combustible supplying mechanism while an amount of combustibles stored in the hopper is controlled so as to be constant. Accordingly, it is possible to reduce a variation of a combustible gas produced in the gasification furnace and facilitate stable operation of the gasification furnace. Further, since a variation of a combustible gas produced is thus reduced, it is also possible to facilitate stable operation of a slagging combustion furnace subsequent to the gasification furnace.
- a combustible supplying apparatus characterized by comprising a relief valve for releasing a combustible gas which leaks from the gasification furnace to a second combustible supplying mechanism side, and supplying means for supplying the combustible gas released through the relief valve to a waste pit.
- a gasification and slagging combustion system having a gasification furnace for gasifying combustibles and a slagging combustion furnace for melting a product produced in the gasification furnace
- the gasification and slagging combustion system is characterized by comprising a first combustible supplying mechanism for supplying the combustibles while preventing external air from leaking into the gasification furnace together with the combustibles, a hopper for storing the combustibles supplied through the first combustible supplying mechanism, and a second combustible supplying mechanism for supplying the combustibles in the hopper to the gasification furnace in fixed quantity while controlling an amount of combustibles stored in the hopper so as to be constant.
- a gasification and slagging combustion system characterized by comprising a relief valve for releasing a combustible gas which leaks from the gasification furnace to a second combustible supplying mechanism side, and supplying means for supplying the combustible gas released through the relief valve to a waste pit.
- FIG 2 is a diagram showing a schematic arrangement of a fluidized-bed gasification furnace and a combustible supplying apparatus for supplying combustibles into the fluidized-bed gasification furnace according to the present invention.
- a combustible supplying means 30 having a screw conveyor 31 operated by a motor 32 is connected to a combustible introduction port 13.
- a combustible supplying means 33 having a screw conveyor 34 operated by a motor 35 is connected to the combustible supplying means 30.
- a hopper 36 is provided so as to be connected to the combustible supplying means 33.
- a chute 37 is provided so as to be connected to the hopper 36.
- a hopper 38 is provided so as to be connected to the chute 37.
- a pusher 39 is provided at a junction between the chute 37 and the hopper 38.
- Combustibles 14 such as municipal wastes, industrial wastes, biomass wastes, medical wastes, or automobile wastes including tire wastes, shredder dust, and the like, are introduced into the hopper 38 by a crane 21 or the like. Material sealing is effectively performed by consolidated combustibles 14, which have been pushed at a lower feeding portion of the hopper by the pusher 39. Combustibles 14 are fed each time in a predetermined amount by the pusher 39 and received by the hopper 36. A level sensor 18 is provided in the hopper 36. The pusher 39 is operated so that the amount of combustibles held in the hopper 36 is maintained to be substantially constant. Material sealing effects provided by the consolidated combustibles 14 at the lower portion of the hopper 38 can prevent leakage of external air. Sealing effects provided by the combustibles 14 piled in the hopper 36 can also prevent entry of external air.
- a pusher 40 is provided at a lower portion of the hopper 36.
- a pusher portion 403 is pushed into the hopper 36 by a driving portion 401 of the pusher 40 to press the combustibles 14 against the screw 34.
- a scraping device 41 is provided at a tip portion of the screw 34. The combustibles 14 pushed by the screw 34 are mechanically scraped to smoothen supply of the combustibles 14 to the screw conveyor 31.
- the combustibles 14 supplied from the combustible supplying means 33 to the combustible supplying means 30 at a constant rate are supplied by the screw conveyor 31 through the combustible introduction port 13 into the fluidized-bed gasification furnace 10.
- the combustibles 14 can be supplied at a constant rate, it is possible to remarkably facilitate stable operation of the fluidized-bed gasification furnace 10 with control of the amount of fluidizing gas 12 to be supplied and control of temperature in the furnace.
- a relief valve 42 is provided in the combustible supplying means 33.
- a combustible gas leaking from the fluidized-bed gasification furnace 10 can be released through the relief valve 42 and introduced to a waste pit by a supplying means having pipes, which is not shown. Since air is continuously drawn from the waste pit for deodorization and used for combustion, the combustible gas can be treated safely.
- a cutoff damper which is not shown, is provided on a chute 43, which interconnects the combustible supplying means 33 and the combustible supplying means 30. The cutoff damper is closed at the beginning of operation or at the time of emergency.
- a combustible gas 17 in the fluidized-bed gasification furnace 10 is prevented from being released through the combustible supplying apparatus to an atmosphere, and the safety of the fluidized-bed gasification furnace 10 can be enhanced.
- the filling density of the combustibles 14 to be received is enhanced by a first combustible supplying mechanism including the hopper 38, the pusher 39, and the chute 37 so as to provide sealing effects to prevent leakage of external air.
- the combustibles 14 intermittently supplied are supplied into the fluidized-bed gasification furnace 10 at a predetermined rate by a second combustible supplying mechanism including the hopper 36, the combustible supplying means 33, and the combustible supplying means 30 while the sealing effects provided by the combustibles 14 are maintained.
- a special sealing mechanism such as a damper.
- FIG 3 shows an embodiment in which the combustible supplying means 30 in FIG 2 is replaced with a chute 43.
- a constant amount of combustibles supplied is achieved by the pusher 40, the screw conveyor 34, and the scraping device 41 of the combustible supplying means 33. Accordingly, the combustible supplying means 30 does not need to supply combustibles at a constant rate. Therefore, in the embodiment shown in FIG 3, the combustible supplying means 30 is eliminated so as to supply combustibles 14 from the combustible supplying means 33 through the chute 43 directly into the fluidized-bed gasification furnace 10. With the structure shown in FIG 3, the chute 43 needs to have a proper inclination angle. Therefore, the entire combustible supplying facility is inevitably located at a high position.
- FIG 4 is a diagram showing a schematic arrangement example of another fluidized-bed gasification furnace and another combustible supplying apparatus according to the present invention.
- the same or corresponding parts are designated by the same reference numerals as those in FIGS. 2 and 3, and details thereof will be omitted.
- details of structures of a waste pit 501, which supplies combustibles 14 into a hopper 38, are illustrated. Specifically, combustibles 14 are delivered through a waste introduction door 502 into the waste pit 501 while outside air is blocked. The combustibles 14 delivered into the waste pit 501 are introduced into the hopper 38 by a crane 21 or the like.
- the internal pressure of the waste pit 501 is maintained to be a negative pressure, so that a gas in the waste pit 501 does not flow out the waste pit 501 (this holds true in the embodiments shown in FIGS. 2 and 3).
- Material sealing is effectively performed to the combustibles 14 in the hopper 38 by consolidated combustibles 14, which have been pushed at a lower portion of the hopper 38 by the pusher 39.
- External air or a gas in the waste pit 501 can be prevented from flowing into the fluidized-bed gasification furnace 10 by material sealing provided by the combustibles 14 consolidated at the lower portion of the hopper 38.
- a predetermined amount of combustibles 14 is fed and introduced into the hopper 36 by the pusher 39.
- So-called spilled wastes produced when the pusher 39 is retracted are delivered and returned to the waste pit 501 by a dedicated conveyor, which is not shown. Since a level sensor 18 is provided in the hopper 36, the pusher 39 can be operated so that the amount of combustibles 14 in the hopper 36 is maintained to a constant value. Material sealing provided by the combustibles 14 in the hopper 36 can also prevent external air from flowing into the fluidized-bed gasification furnace 10.
- a pusher portion 403 is pushed into the hopper 36 by a driving portion 401 of the pusher 40 to press the combustibles 14 against the screw 34, as with the effects of the pusher 40 shown in FIG 2.
- a scraping device 41 is provided at an outlet of the screw 34.
- the combustibles 14 pushed by the screw 34 are mechanically scraped to make supply of the screw 34 constant more effectively.
- the combustibles 14 which have passed the scraping device 41 are supplied through the chute 43 into the fluidized-bed gasification furnace 10.
- a relief valve 42 is provided in the combustible supplying means 33 so that a combustible gas leaking from the fluidized-bed gasification furnace 10 is released from the relief valve 42 through a pipe (supplying means) 500 into the waste pit 501 when the interior of the fluidized-bed gasification furnace 10 has a positive pressure.
- a path such that the combustible gas leaking from the fluidized-bed gasification furnace 10 is drawn from the relief valve 42 by a blower and introduced directly into a combustion gas pipe 700.
- a gas in the waste pit 501 is continuously drawn by a forced draft blower 504.
- the amount of gas drawn can be adjusted by a valve 503. It is desirable that the gas introduced into the combustion gas pipe 700 is mixed with air separately introduced from an external space and then used as combustion air for the fluidized-bed gasification furnace 10 and/or a slagging combustion furnace in a gasification and slagging combustion system.
- an emergency shutoff valve 44 is provided in the chute 43, and that the emergency shutoff valve 44 is closed at the time of emergency or at the beginning of operation, because it is possible to prevent a combustible gas in the fluidized-bed gasification furnace 10 from leaking out through the combustible supplying apparatus to the exterior of the system.
- FIG 5 is a schematic diagram showing an example of an entire system in which a combustible supplying apparatus according to the present invention is applied to a gasification and slagging combustion system.
- the gasification and slagging combustion system is defined as a system which gasifies combustibles in a gasification furnace, introduces products such as gas, char, tar produced in the gasification furnace into a slagging combustion furnace, and combusts the products at a high temperature in the slagging combustion furnace to melt ash content contained in the products into slag.
- the gasification and slagging combustion system will be described with reference to FIG 5.
- a combustible gas 17 as a product produced in a fluidized-bed gasification furnace 10 is introduced into a slagging combustion furnace 800 so as to form a circulating flow in the slagging combustion furnace 800.
- Combustion air 801 is introduced in tangential directions of the circulating flow to convert ash content into slag mist.
- the slag mist is trapped on furnace walls by circulating effect of the gas.
- the molten slag discharged through a slag discharge port 802 is converted into water granulated slag in a water chamber 803 and discharged to the exterior of the system by a conveyor 804.
- heat of a combustion exhaust gas produced in the slagging combustion furnace 800 is recovered as steam by a waste heat boiler 900, and the combustion exhaust gas is cooled in a gas cooling chamber 901. After fly ash is collected by a bag filter 902, the combustion exhaust gas is discharged to the exterior of the system.
- the entire gasification and slagging combustion system is maintained at a negative pressure by an induced draft fan 903.
- Such a gasification and slagging combustion system may employ a combustible supplying apparatus shown in FIG 2 or 3.
- the use of a combustible supplying apparatus which can prevent external air from leaking into a gasification furnace and does not require any mechanical sealing mechanisms such as a double damper can allow a gasification and slagging combustion system to be operated extremely safely. Furthermore, improvement of sealing and improvement of constant supply have heretofore been antinomic problems.
- the use of a supplying apparatus according to the present invention can achieve a combustible supplying method which is superior in sealing effects and constant supply. Further, even if a combustible gas leaks through the combustible supplying apparatus, the present system can treat the combustible gas safely.
- combustibles are supplied to a hopper while external air is prevented from leaking into the gasification furnace together with the combustibles.
- a method of supplying combustibles to a gasification furnace which can prevent external air from leaking into the gasification furnace and does not require any special sealing mechanisms such as a double damper.
- the combustibles in the hopper are supplied to the gasification furnace in fixed quantity while an amount of stored combustibles supplied to the hopper is controlled so as to be constant.
- combustibles are supplied to a hopper by a first combustible supplying mechanism while external air is prevented from leaking into the gasification furnace.
- a combustible supplying apparatus for supplying combustibles to a gasification furnace and a gasification and slagging combustion system which can prevent external air from leaking into the gasification furnace and does not require any special sealing mechanisms such as a double damper.
- the combustibles in the hopper are supplied to the gasification furnace in fixed quantity while an amount of stored combustibles supplied to the hopper is controlled so as to be constant.
- a combustible supplying apparatus for supplying combustibles to a gasification furnace and a gasification and slagging combustion system which can release, through a relief valve, a combustible gas which leaks from the gasification furnace when the gasification furnace has a positive pressure and can introduce the combustible gas to a waste pit by supplying means. Because air is continuously drawn from the waste pit and used for combustion, a combustible gas can be treated safely.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Gasification And Melting Of Waste (AREA)
- Incineration Of Waste (AREA)
Abstract
Description
- The present invention relates to a method and apparatus for supplying combustibles, such as municipal wastes, industrial wastes, biomass wastes, medical wastes, or automobile wastes including tire wastes, shredder dust, and the like, to a gasification furnace which gasifies the combustibles into a combustible gas, and to a gasification and slagging combustion system.
- In recent years, in order to treat combustibles, such as municipal wastes, industrial wastes, biomass wastes, medical wastes, or automobile wastes including tire wastes, shredder dust, and the like, there has been known a gasification and slagging combustion facility which gasifies the combustibles under a reducing atmosphere in a gasification furnace and combusts a combustible gas produced by the gasification at a high temperature in a slagging combustion furnace to combust an unburned combustible carbon content such as char accompanying the combustible gas, and simultaneously to melt ash content contained in the char into slag.
- FIG 1 is a diagram showing a schematic arrangement example of a fluidized-bed gasification furnace and a combustible supplying apparatus for supplying combustibles into the fluidized-bed gasification furnace which are used in this type of gasification and slagging combustion facility. As shown in FIG 1, the fluidized-
bed gasification furnace 10 holds a fluidized medium at a lower portion thereof, and a fluidizedbed 11 of the fluidized medium is formed by supplying a fluidizinggas 12 from a lower portion of the furnace. -
Combustibles 14 introduced through acombustible introduction port 13 are gasified by partial combustion under a reducing atmosphere in the fluidizedbed 11. A producedcombustible gas 17 flows upward in the fluidizedbed 11, passes through afreeboard 15, is introduced through a combustiblegas outlet port 16 into a slagging combustion furnace, which is not shown, and is combusted at a high temperature. - This type of fluidized-
bed gasification furnace 10 is generally operated so that the pressure in the furnace is a negative pressure of about -50 mm Aq. Accordingly, a large amount of external air which has not been preheated leaks through thecombustible introduction port 13 into the furnace. The leaked air which has not been preheated is consumed by combustion at thefreeboard 15 in the fluidized-bed gasification furnace 10. The combustible gas combusted in part by the leaked air is introduced through the combustiblegas outlet port 16 into the slagging combustion furnace. Combustion air to be supplied to the slagging combustion furnace is generally preheated so as to increase the temperature of the slagging combustion furnace. However, if the aforementioned leaked air is introduced into the slagging combustion furnace, the amount of preheated air supplied to the slagging combustion furnace is reduced. As a result, the melting temperature is lowered. Further, when the pressure in the fluidized-bed gasification furnace 10 becomes a positive pressure for some reasons, it is necessary to prevent the combustible gas in the fluidized-bed gasification furnace 10 from leaking to the combustible supplying apparatus. Therefore, for example, dampers having a sealing function (so-called double damper) are doubly provided in a chute connected to the combustible introduction port 13 (which corresponds to a portion between acombustible supplying means 30 and acombustible supplying means 33 connected to an upper stage of thecombustible supplying means 30 in FIG 1) andcombustibles 14 introduced into ahopper 38 by acrane 21 are supplied through thedouble damper 19 into thecombustible supplying means 30 by ascrew 34 while external air is prevented from entering the fluidized-bed gasification furnace 10 through thecombustible introduction port 13 by sealing effects of thedouble damper 19. - However, with a method of intermittently supplying
combustibles 14 into the fluidized-bed gasification furnace 10 as described above, because heat is extremely promptly transferred to the suppliedcombustibles 14 in the fluidizedbed 11, the amount ofcombustible gas 17 produced in the fluidized-bed gasification furnace 10 is greatly varied under the influence of intermittent supply of thecombustibles 14. Thus, stable operation of the fluidized-bed gasification furnace 10 is hindered, and operational control for the subsequent slagging combustion furnace to receive a produced gas from the fluidized-bed gasification furnace 10 and combust the produced gas under a high temperature at a low excess air ratio is also hindered. - Further, since the
hopper 38 is intermittently supplied withcombustibles 14, the amount ofcombustibles 14 stored in thehopper 38 has large variations. Furthermore,combustibles 14 themselves have variations in quality. Therefore, fixed quantity supply cannot necessarily be achieved by thescrew 34. - The present invention has been made in view of the above drawbacks, and it is, therefore, an object of the present invention to provide a method and apparatus for supplying combustibles to a gasification furnace and to a gasification and slagging combustion system which can prevent leakage of external air into the gasification furnace, reduce a variation of a produced gas, and facilitate operational control for stable gasification.
- According to the present invention, there is provided a method of supplying combustibles to a gasification furnace for gasifying the combustibles, and the method is characterized by comprising supplying the combustibles to a hopper while preventing external air from leaking into the gasification furnace by the combustibles themselves, and supplying the combustibles in the hopper to the gasification furnace in fixed quantity while controlling an amount of combustibles stored in the hopper so as to be constant. As described above, combustibles are supplied to a hopper while external air is prevented from leaking into the gasification furnace together with the combustibles by the combustibles. Thus, external air can be prevented from leaking into the gasification furnace, and it is not necessary to provide any special sealing mechanisms such as a double damper. Simultaneously, the combustibles in the hopper are supplied to the gasification furnace in fixed quantity while an amount of combustibles stored in the hopper is controlled so as to be constant. Accordingly, it is possible to reduce a variation of a combustible gas produced in the gasification furnace and facilitate stable operation of the gasification furnace. Further, since a variation of a combustible gas produced is thus reduced, it is also possible to facilitate stable operation of a slagging combustion furnace subsequent to the gasification furnace.
- According to the present invention, there is provided a method characterized in that a combustible gas which leaks from the gasification furnace to a combustible supplying side is released to a waste pit. A combustible gas which leaks from the gasification furnace to a combustible supplying side can be treated safely by releasing the combustible gas to a waste pit because air is continuously drawn from the waste pit for deodorization and used for combustion.
- According to the present invention, there is provided a combustible supplying apparatus for supplying combustibles to a gasification furnace for gasifying the combustibles, and the combustible supplying apparatus is characterized by comprising a first combustible supplying mechanism for supplying the combustibles while preventing external air from leaking into the gasification furnace, a hopper for storing the combustibles supplied through the first combustible supplying mechanism, and a second combustible supplying mechanism for supplying the combustibles in the hopper to the gasification furnace in fixed quantity while controlling an amount of combustibles stored in the hopper so as to be constant. As described above, combustibles are supplied to a hopper by the first combustible supplying mechanism while external air is prevented from leaking into the gasification furnace. Thus, external air can be prevented from leaking into the gasification furnace, and it is not necessary to provide any special sealing mechanisms such as a double damper. Simultaneously, the combustibles in the hopper are supplied to the gasification furnace in fixed quantity by the second combustible supplying mechanism while an amount of combustibles stored in the hopper is controlled so as to be constant. Accordingly, it is possible to reduce a variation of a combustible gas produced in the gasification furnace and facilitate stable operation of the gasification furnace. Further, since a variation of a combustible gas produced is thus reduced, it is also possible to facilitate stable operation of a slagging combustion furnace subsequent to the gasification furnace.
- According to the present invention, there is provided a combustible supplying apparatus characterized by comprising a relief valve for releasing a combustible gas which leaks from the gasification furnace to a second combustible supplying mechanism side, and supplying means for supplying the combustible gas released through the relief valve to a waste pit. With a relief valve thus provided, a combustible gas which leaks from the gasification furnace when the gasification furnace has a positive pressure can be released through a relief valve, and the combustible gas can be introduced to a waste pit by supplying means. Air is continuously drawn from the waste pit for deodorization and used for combustion, so that a combustible gas can be treated safely.
- According to the present invention, there is provided a gasification and slagging combustion system having a gasification furnace for gasifying combustibles and a slagging combustion furnace for melting a product produced in the gasification furnace, and the gasification and slagging combustion system is characterized by comprising a first combustible supplying mechanism for supplying the combustibles while preventing external air from leaking into the gasification furnace together with the combustibles, a hopper for storing the combustibles supplied through the first combustible supplying mechanism, and a second combustible supplying mechanism for supplying the combustibles in the hopper to the gasification furnace in fixed quantity while controlling an amount of combustibles stored in the hopper so as to be constant.
- According to the present invention, there is provided a gasification and slagging combustion system characterized by comprising a relief valve for releasing a combustible gas which leaks from the gasification furnace to a second combustible supplying mechanism side, and supplying means for supplying the combustible gas released through the relief valve to a waste pit.
-
- FIG 1 is a diagram showing a schematic arrangement example of a conventional fluidized-bed gasification furnace and a conventional combustible supplying apparatus;
- FIG 2 is a diagram showing a schematic arrangement example of a fluidized-bed gasification furnace and a combustible supplying apparatus according to an embodiment of the present invention;
- FIG 3 is a diagram showing a schematic arrangement example of a fluidized-bed gasification furnace and a combustible supplying apparatus according to another embodiment of the present invention;
- FIG 4 is a diagram showing a schematic arrangement example of a fluidized-bed gasification furnace and a combustible supplying apparatus according to another embodiment of the present invention; and
- FIG 5 is a schematic diagram showing an example of an entire system in which a combustible supplying apparatus according to the present invention is applied to a gasification and slagging combustion system.
- FIG 2 is a diagram showing a schematic arrangement of a fluidized-bed gasification furnace and a combustible supplying apparatus for supplying combustibles into the fluidized-bed gasification furnace according to the present invention. In FIG 2, parts designated by the same reference numerals as those in FIG 1 denote the same or corresponding parts. This also holds true in other drawings. In FIG 2, a combustible supplying means 30 having a
screw conveyor 31 operated by amotor 32 is connected to acombustible introduction port 13. A combustible supplying means 33 having ascrew conveyor 34 operated by amotor 35 is connected to thecombustible supplying means 30. Ahopper 36 is provided so as to be connected to thecombustible supplying means 33. Achute 37 is provided so as to be connected to thehopper 36. Ahopper 38 is provided so as to be connected to thechute 37. Apusher 39 is provided at a junction between thechute 37 and thehopper 38. -
Combustibles 14, such as municipal wastes, industrial wastes, biomass wastes, medical wastes, or automobile wastes including tire wastes, shredder dust, and the like, are introduced into thehopper 38 by acrane 21 or the like. Material sealing is effectively performed by consolidatedcombustibles 14, which have been pushed at a lower feeding portion of the hopper by thepusher 39.Combustibles 14 are fed each time in a predetermined amount by thepusher 39 and received by thehopper 36. Alevel sensor 18 is provided in thehopper 36. Thepusher 39 is operated so that the amount of combustibles held in thehopper 36 is maintained to be substantially constant. Material sealing effects provided by the consolidatedcombustibles 14 at the lower portion of thehopper 38 can prevent leakage of external air. Sealing effects provided by thecombustibles 14 piled in thehopper 36 can also prevent entry of external air. - A
pusher 40 is provided at a lower portion of thehopper 36. Apusher portion 403 is pushed into thehopper 36 by a drivingportion 401 of thepusher 40 to press thecombustibles 14 against thescrew 34. Thus, local consolidation of thecombustibles 14 is prevented, and thecombustibles 14 can reliably be discharged by thescrew 34. Ascraping device 41 is provided at a tip portion of thescrew 34. Thecombustibles 14 pushed by thescrew 34 are mechanically scraped to smoothen supply of thecombustibles 14 to thescrew conveyor 31. - The
combustibles 14 supplied from the combustible supplyingmeans 33 to the combustible supplyingmeans 30 at a constant rate are supplied by thescrew conveyor 31 through thecombustible introduction port 13 into the fluidized-bed gasification furnace 10. Thus, since thecombustibles 14 can be supplied at a constant rate, it is possible to remarkably facilitate stable operation of the fluidized-bed gasification furnace 10 with control of the amount of fluidizinggas 12 to be supplied and control of temperature in the furnace. - It is desirable that a
relief valve 42 is provided in the combustible supplyingmeans 33. When the fluidized-bed gasification furnace 10 has a positive pressure (a pressure higher than an atmospheric pressure), a combustible gas leaking from the fluidized-bed gasification furnace 10 can be released through therelief valve 42 and introduced to a waste pit by a supplying means having pipes, which is not shown. Since air is continuously drawn from the waste pit for deodorization and used for combustion, the combustible gas can be treated safely. A cutoff damper, which is not shown, is provided on achute 43, which interconnects the combustible supplyingmeans 33 and the combustible supplyingmeans 30. The cutoff damper is closed at the beginning of operation or at the time of emergency. Thus, acombustible gas 17 in the fluidized-bed gasification furnace 10 is prevented from being released through the combustible supplying apparatus to an atmosphere, and the safety of the fluidized-bed gasification furnace 10 can be enhanced. - In the combustible supplying apparatus shown in FIG 2, the filling density of the
combustibles 14 to be received is enhanced by a first combustible supplying mechanism including thehopper 38, thepusher 39, and thechute 37 so as to provide sealing effects to prevent leakage of external air. Simultaneously, thecombustibles 14 intermittently supplied are supplied into the fluidized-bed gasification furnace 10 at a predetermined rate by a second combustible supplying mechanism including thehopper 36, the combustible supplyingmeans 33, and the combustible supplyingmeans 30 while the sealing effects provided by thecombustibles 14 are maintained. Further, since leakage of external air into the fluidized-bed gasification furnace 10 is prevented by the above material sealing, it is not necessary to provide a special sealing mechanism such as a damper. - FIG 3 shows an embodiment in which the combustible supplying
means 30 in FIG 2 is replaced with achute 43. A constant amount of combustibles supplied is achieved by thepusher 40, thescrew conveyor 34, and thescraping device 41 of the combustible supplyingmeans 33. Accordingly, the combustible supplyingmeans 30 does not need to supply combustibles at a constant rate. Therefore, in the embodiment shown in FIG 3, the combustible supplyingmeans 30 is eliminated so as to supplycombustibles 14 from the combustible supplyingmeans 33 through thechute 43 directly into the fluidized-bed gasification furnace 10. With the structure shown in FIG 3, thechute 43 needs to have a proper inclination angle. Therefore, the entire combustible supplying facility is inevitably located at a high position. - FIG 4 is a diagram showing a schematic arrangement example of another fluidized-bed gasification furnace and another combustible supplying apparatus according to the present invention. In this embodiment, the same or corresponding parts are designated by the same reference numerals as those in FIGS. 2 and 3, and details thereof will be omitted. In this embodiment, details of structures of a
waste pit 501, which suppliescombustibles 14 into ahopper 38, are illustrated. Specifically,combustibles 14 are delivered through awaste introduction door 502 into thewaste pit 501 while outside air is blocked. Thecombustibles 14 delivered into thewaste pit 501 are introduced into thehopper 38 by acrane 21 or the like. The internal pressure of thewaste pit 501 is maintained to be a negative pressure, so that a gas in thewaste pit 501 does not flow out the waste pit 501 (this holds true in the embodiments shown in FIGS. 2 and 3). Material sealing is effectively performed to thecombustibles 14 in thehopper 38 byconsolidated combustibles 14, which have been pushed at a lower portion of thehopper 38 by thepusher 39. External air or a gas in thewaste pit 501 can be prevented from flowing into the fluidized-bed gasification furnace 10 by material sealing provided by thecombustibles 14 consolidated at the lower portion of thehopper 38. A predetermined amount ofcombustibles 14 is fed and introduced into thehopper 36 by thepusher 39. So-called spilled wastes produced when thepusher 39 is retracted are delivered and returned to thewaste pit 501 by a dedicated conveyor, which is not shown. Since alevel sensor 18 is provided in thehopper 36, thepusher 39 can be operated so that the amount ofcombustibles 14 in thehopper 36 is maintained to a constant value. Material sealing provided by thecombustibles 14 in thehopper 36 can also prevent external air from flowing into the fluidized-bed gasification furnace 10. - With regard to effects of the
pusher 40, apusher portion 403 is pushed into thehopper 36 by a drivingportion 401 of thepusher 40 to press thecombustibles 14 against thescrew 34, as with the effects of thepusher 40 shown in FIG 2. Thus, local consolidation of thecombustibles 14 is prevented, and constant supply into thescrew 34 can be maintained. Ascraping device 41 is provided at an outlet of thescrew 34. Thecombustibles 14 pushed by thescrew 34 are mechanically scraped to make supply of thescrew 34 constant more effectively. Thecombustibles 14 which have passed thescraping device 41 are supplied through thechute 43 into the fluidized-bed gasification furnace 10. - Further, a
relief valve 42 is provided in the combustible supplyingmeans 33 so that a combustible gas leaking from the fluidized-bed gasification furnace 10 is released from therelief valve 42 through a pipe (supplying means) 500 into thewaste pit 501 when the interior of the fluidized-bed gasification furnace 10 has a positive pressure. There may be provided a path such that the combustible gas leaking from the fluidized-bed gasification furnace 10 is drawn from therelief valve 42 by a blower and introduced directly into acombustion gas pipe 700. A gas in thewaste pit 501 is continuously drawn by a forceddraft blower 504. The amount of gas drawn can be adjusted by avalve 503. It is desirable that the gas introduced into thecombustion gas pipe 700 is mixed with air separately introduced from an external space and then used as combustion air for the fluidized-bed gasification furnace 10 and/or a slagging combustion furnace in a gasification and slagging combustion system. - From the viewpoint of safety, it is desirable that an
emergency shutoff valve 44 is provided in thechute 43, and that theemergency shutoff valve 44 is closed at the time of emergency or at the beginning of operation, because it is possible to prevent a combustible gas in the fluidized-bed gasification furnace 10 from leaking out through the combustible supplying apparatus to the exterior of the system. - FIG 5 is a schematic diagram showing an example of an entire system in which a combustible supplying apparatus according to the present invention is applied to a gasification and slagging combustion system. The gasification and slagging combustion system is defined as a system which gasifies combustibles in a gasification furnace, introduces products such as gas, char, tar produced in the gasification furnace into a slagging combustion furnace, and combusts the products at a high temperature in the slagging combustion furnace to melt ash content contained in the products into slag. The gasification and slagging combustion system will be described with reference to FIG 5. A
combustible gas 17 as a product produced in a fluidized-bed gasification furnace 10 is introduced into a slaggingcombustion furnace 800 so as to form a circulating flow in the slaggingcombustion furnace 800.Combustion air 801 is introduced in tangential directions of the circulating flow to convert ash content into slag mist. The slag mist is trapped on furnace walls by circulating effect of the gas. The molten slag discharged through aslag discharge port 802 is converted into water granulated slag in awater chamber 803 and discharged to the exterior of the system by aconveyor 804. On the other hand, heat of a combustion exhaust gas produced in the slaggingcombustion furnace 800 is recovered as steam by awaste heat boiler 900, and the combustion exhaust gas is cooled in agas cooling chamber 901. After fly ash is collected by abag filter 902, the combustion exhaust gas is discharged to the exterior of the system. The entire gasification and slagging combustion system is maintained at a negative pressure by an induceddraft fan 903. - Such a gasification and slagging combustion system may employ a combustible supplying apparatus shown in FIG 2 or 3.
- With the above arrangement, the use of a combustible supplying apparatus which can prevent external air from leaking into a gasification furnace and does not require any mechanical sealing mechanisms such as a double damper can allow a gasification and slagging combustion system to be operated extremely safely. Furthermore, improvement of sealing and improvement of constant supply have heretofore been antinomic problems. However, the use of a supplying apparatus according to the present invention can achieve a combustible supplying method which is superior in sealing effects and constant supply. Further, even if a combustible gas leaks through the combustible supplying apparatus, the present system can treat the combustible gas safely.
- As described above, according to the present invention as recited in
claims 1 and 2, combustibles are supplied to a hopper while external air is prevented from leaking into the gasification furnace together with the combustibles. Thus, it is possible to provide a method of supplying combustibles to a gasification furnace which can prevent external air from leaking into the gasification furnace and does not require any special sealing mechanisms such as a double damper. Simultaneously, the combustibles in the hopper are supplied to the gasification furnace in fixed quantity while an amount of stored combustibles supplied to the hopper is controlled so as to be constant. Accordingly, it is possible to reduce a variation of a combustible gas produced in the gasification furnace and facilitate stable operation of the gasification furnace. Further, since a variation of a combustible gas produced is thus reduced, it is also possible to facilitate stable operation of a slagging combustion furnace subsequent to the gasification furnace. - According to the present invention as recited in claim 2, it is possible to provide a method of supplying combustibles to a gasification furnace which can treat a combustible gas safely by releasing, to a waste pit, a combustible gas which leaks from the gasification furnace to a combustible supplying side because air is continuously drawn from the waste pit and used for combustion.
- According to the present invention as recited in claims 3 and 5, combustibles are supplied to a hopper by a first combustible supplying mechanism while external air is prevented from leaking into the gasification furnace. Thus, it is possible to provide a combustible supplying apparatus for supplying combustibles to a gasification furnace and a gasification and slagging combustion system which can prevent external air from leaking into the gasification furnace and does not require any special sealing mechanisms such as a double damper. Simultaneously, the combustibles in the hopper are supplied to the gasification furnace in fixed quantity while an amount of stored combustibles supplied to the hopper is controlled so as to be constant. Accordingly, it is possible to reduce a variation of a combustible gas produced in the gasification furnace and facilitate stable operation of the gasification furnace. Further, since a variation of a combustible gas produced is thus reduced, it is also possible to facilitate stable operation of a slagging combustion furnace subsequent to the gasification furnace.
- According to the present invention as recited in claims 4 and 6, it is possible to provide a combustible supplying apparatus for supplying combustibles to a gasification furnace and a gasification and slagging combustion system which can release, through a relief valve, a combustible gas which leaks from the gasification furnace when the gasification furnace has a positive pressure and can introduce the combustible gas to a waste pit by supplying means. Because air is continuously drawn from the waste pit and used for combustion, a combustible gas can be treated safely.
Claims (6)
- A method of supplying combustibles to a gasification furnace for gasifying the combustibles, said method characterized by comprising:supplying the combustibles to a hopper while preventing external air from leaking into the gasification furnace by the combustibles; andsupplying the combustibles in said hopper to the gasification furnace in fixed quantity while controlling an amount of combustibles stored in said hopper so as to be constant.
- The method of supplying combustibles to a gasification furnace as recited in claim 1, characterized in that a combustible gas which leaks from the gasification furnace to a combustible supplying side is released to a waste pit.
- A combustible supplying apparatus for supplying combustibles to a gasification furnace for gasifying the combustibles, said combustible supplying apparatus characterized by comprising:a first combustible supplying mechanism for supplying the combustibles while preventing external air from leaking into the gasification furnace by the combustibles;a hopper for storing the combustibles supplied through said first combustible supplying mechanism; anda second combustible supplying mechanism for supplying the combustibles in said hopper to the gasification furnace in fixed quantity while controlling an amount of combustibles stored in said hopper so as to be constant.
- The combustible supplying apparatus for supplying combustibles to a gasification furnace as recited in claim 3, said combustible supplying apparatus characterized by comprising a relief valve for releasing a combustible gas which leaks from the gasification furnace to a combustible supplying side, and supplying means for supplying the combustible gas released through said relief valve to a waste pit.
- A gasification and slagging combustion system having a gasification furnace for gasifying combustibles and a slagging combustion furnace for melting a product produced in said gasification furnace, said gasification and slagging combustion system characterized by comprising:a first combustible supplying mechanism for supplying the combustibles while preventing external air from leaking into said gasification furnace together with the combustibles;a hopper for storing the combustibles supplied through said first combustible supplying mechanism; anda second combustible supplying mechanism for supplying the combustibles in said hopper to said gasification furnace in fixed quantity while controlling an amount of combustibles stored in said hopper so as to be constant.
- The gasification and slagging combustion system as recited in claim 5, characterized by comprising a relief valve for releasing a combustible gas which leaks from the gasification furnace to a second combustible supplying mechanism side, and supplying means for supplying the combustible gas released through said relief valve to a waste pit.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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PCT/JP2003/001736 WO2004074409A1 (en) | 2003-02-18 | 2003-02-18 | Method and device for feeding inflammables to gasifying furnace, and gasification melting system |
Publications (2)
Publication Number | Publication Date |
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EP1736527A1 true EP1736527A1 (en) | 2006-12-27 |
EP1736527A4 EP1736527A4 (en) | 2006-12-27 |
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EP03706956A Withdrawn EP1736527A4 (en) | 2003-02-18 | 2003-02-18 | Method and device for feeding inflammables to gasifying furnace, and gasification melting system |
Country Status (5)
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EP (1) | EP1736527A4 (en) |
JP (1) | JPWO2004074409A1 (en) |
AU (1) | AU2003211226A1 (en) |
TW (1) | TW200506278A (en) |
WO (1) | WO2004074409A1 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007113497A1 (en) * | 2006-04-06 | 2007-10-11 | Peter Stein | Hybrid feed mechanism |
WO2007103771A3 (en) * | 2006-03-06 | 2008-01-31 | Robert E Klepper | Method and apparatus for producing synthesis gas from waste materials |
US8182561B2 (en) | 2008-01-16 | 2012-05-22 | Shell Oil Company | Process to provide a particulate solid material to a pressurised reactor |
EP2685166A1 (en) * | 2011-03-11 | 2014-01-15 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. | Garbage supply device |
EP2693119A1 (en) * | 2011-03-28 | 2014-02-05 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. | Waste material supply device and waste material processing device |
JP2014181843A (en) * | 2013-03-19 | 2014-09-29 | Dowa Eco-System Co Ltd | Powdery waste supply apparatus, and method for supplying powdery waste |
EP2833062A4 (en) * | 2012-03-30 | 2015-11-25 | Hangzhou Hengming Environmental Technology Co Ltd | SYSTEM OF TREATMENT AND USE OF SOLID WASTE WASTE |
EP2180255A4 (en) * | 2007-08-21 | 2015-12-23 | Kobelco Eco Solutions Co Ltd | WASTE SUPPLY DEVICE, METHOD OF SEPARATING AND WASTE TRANSFER METHOD |
EP2534424A4 (en) * | 2010-02-10 | 2017-11-29 | KiOR, Inc. | Improved biomass feed system/process |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007255816A (en) * | 2006-03-24 | 2007-10-04 | Mitsubishi Heavy Ind Ltd | Waste supply device and waste treatment device |
JP5421051B2 (en) * | 2009-10-08 | 2014-02-19 | 株式会社大川原製作所 | Incineration equipment and incineration equipment operation method |
CN103528066B (en) * | 2012-07-05 | 2016-01-27 | 蒋华俊 | Refuse disposal installation |
CN112146107A (en) * | 2020-11-09 | 2020-12-29 | 郑宗标 | Medical waste incinerator |
JP7587798B2 (en) | 2021-12-14 | 2024-11-21 | カナデビア株式会社 | Waste incineration facility |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4111665A (en) * | 1975-09-09 | 1978-09-05 | Steag A.G. | Apparatus for the gasification under pressure of bituminous coal, especially of fine coal in a generator |
US4140228A (en) * | 1977-12-01 | 1979-02-20 | The United States Of America As Represented By The United States Department Of Energy | Dry piston coal feeder |
WO1999034662A1 (en) * | 1998-01-06 | 1999-07-15 | Emery Recycling Corporation | Apparatus and method for introducing compressible fuel into a gasifier |
WO2003012013A1 (en) * | 2001-08-02 | 2003-02-13 | T.G.E. Tech. Ltd. | Method and apparatus for the treatment of domestic waste |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001279264A (en) * | 2000-03-29 | 2001-10-10 | Toshiba Corp | Thermal cracking furnace unit |
JP2001289422A (en) * | 2000-04-10 | 2001-10-19 | Babcock Hitachi Kk | Gasifying process system |
JP2003056822A (en) * | 2001-08-16 | 2003-02-26 | Ebara Corp | Supply method and apparatus for combustible substance in fluidized bed gasifying furnace |
-
2003
- 2003-02-18 EP EP03706956A patent/EP1736527A4/en not_active Withdrawn
- 2003-02-18 JP JP2004568462A patent/JPWO2004074409A1/en active Pending
- 2003-02-18 WO PCT/JP2003/001736 patent/WO2004074409A1/en active Search and Examination
- 2003-02-18 AU AU2003211226A patent/AU2003211226A1/en not_active Abandoned
-
2004
- 2004-02-17 TW TW093103709A patent/TW200506278A/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4111665A (en) * | 1975-09-09 | 1978-09-05 | Steag A.G. | Apparatus for the gasification under pressure of bituminous coal, especially of fine coal in a generator |
US4140228A (en) * | 1977-12-01 | 1979-02-20 | The United States Of America As Represented By The United States Department Of Energy | Dry piston coal feeder |
WO1999034662A1 (en) * | 1998-01-06 | 1999-07-15 | Emery Recycling Corporation | Apparatus and method for introducing compressible fuel into a gasifier |
WO2003012013A1 (en) * | 2001-08-02 | 2003-02-13 | T.G.E. Tech. Ltd. | Method and apparatus for the treatment of domestic waste |
Non-Patent Citations (1)
Title |
---|
See also references of WO2004074409A1 * |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007103771A3 (en) * | 2006-03-06 | 2008-01-31 | Robert E Klepper | Method and apparatus for producing synthesis gas from waste materials |
WO2007113497A1 (en) * | 2006-04-06 | 2007-10-11 | Peter Stein | Hybrid feed mechanism |
US8100066B2 (en) | 2006-04-06 | 2012-01-24 | Peter Stein | Hybrid feed mechanism |
EP2180255A4 (en) * | 2007-08-21 | 2015-12-23 | Kobelco Eco Solutions Co Ltd | WASTE SUPPLY DEVICE, METHOD OF SEPARATING AND WASTE TRANSFER METHOD |
US9149779B2 (en) | 2008-01-16 | 2015-10-06 | Shell Oil Company | Process to provide a particulate solid material to a pressurised reactor |
US8182561B2 (en) | 2008-01-16 | 2012-05-22 | Shell Oil Company | Process to provide a particulate solid material to a pressurised reactor |
EP2534424A4 (en) * | 2010-02-10 | 2017-11-29 | KiOR, Inc. | Improved biomass feed system/process |
EP2685166A4 (en) * | 2011-03-11 | 2015-04-01 | Mitsubishi Heavy Ind Environmental & Chemical Eng Co Ltd | Garbage supply device |
EP2685166A1 (en) * | 2011-03-11 | 2014-01-15 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. | Garbage supply device |
US9869472B2 (en) | 2011-03-11 | 2018-01-16 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. | Garbage supply device |
EP2693119A1 (en) * | 2011-03-28 | 2014-02-05 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. | Waste material supply device and waste material processing device |
EP2693119A4 (en) * | 2011-03-28 | 2014-10-08 | Mitsubishi Heavy Ind Environmental & Chemical Eng Co Ltd | Waste material supply device and waste material processing device |
US9702553B2 (en) | 2011-03-28 | 2017-07-11 | Mitsubishi Heavy Industries Environmental & Chemical Engineering Co., Ltd. | Waste material supply device and waste material processing device |
EP2833062A4 (en) * | 2012-03-30 | 2015-11-25 | Hangzhou Hengming Environmental Technology Co Ltd | SYSTEM OF TREATMENT AND USE OF SOLID WASTE WASTE |
JP2014181843A (en) * | 2013-03-19 | 2014-09-29 | Dowa Eco-System Co Ltd | Powdery waste supply apparatus, and method for supplying powdery waste |
Also Published As
Publication number | Publication date |
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AU2003211226A1 (en) | 2004-09-09 |
JPWO2004074409A1 (en) | 2006-06-01 |
WO2004074409A1 (en) | 2004-09-02 |
TW200506278A (en) | 2005-02-16 |
EP1736527A4 (en) | 2006-12-27 |
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