EP3540031B1 - Verfahren und vorrichtung zur vergasung durch kombination aus zirkulierendem wirbelbett und pyrolysebett - Google Patents
Verfahren und vorrichtung zur vergasung durch kombination aus zirkulierendem wirbelbett und pyrolysebett Download PDFInfo
- Publication number
- EP3540031B1 EP3540031B1 EP17893195.2A EP17893195A EP3540031B1 EP 3540031 B1 EP3540031 B1 EP 3540031B1 EP 17893195 A EP17893195 A EP 17893195A EP 3540031 B1 EP3540031 B1 EP 3540031B1
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- EP
- European Patent Office
- Prior art keywords
- gasification furnace
- circulating fluidized
- fluidized bed
- bed gasification
- pipe
- Prior art date
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- 238000002309 gasification Methods 0.000 title claims description 187
- 238000000197 pyrolysis Methods 0.000 title claims description 73
- 238000000034 method Methods 0.000 title claims description 11
- 239000007789 gas Substances 0.000 claims description 65
- 239000003245 coal Substances 0.000 claims description 58
- 238000009826 distribution Methods 0.000 claims description 47
- 239000003034 coal gas Substances 0.000 claims description 45
- 239000010881 fly ash Substances 0.000 claims description 42
- 239000002893 slag Substances 0.000 claims description 32
- 230000008021 deposition Effects 0.000 claims description 28
- 239000000203 mixture Substances 0.000 claims description 27
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 25
- 229910052799 carbon Inorganic materials 0.000 claims description 25
- 239000003795 chemical substances by application Substances 0.000 claims description 22
- 238000004891 communication Methods 0.000 claims description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 17
- 229910052760 oxygen Inorganic materials 0.000 claims description 17
- 239000001301 oxygen Substances 0.000 claims description 17
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 2
- 239000003344 environmental pollutant Substances 0.000 description 7
- 231100000719 pollutant Toxicity 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 239000000571 coke Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Images
Classifications
-
- 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
- C10J3/54—Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
- C10J3/56—Apparatus; Plants
-
- 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
- C10J3/54—Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
-
- 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
- C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
- C10J3/60—Processes
-
- 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
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
-
- 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
- C10J2200/152—Nozzles or lances for introducing gas, liquids or suspensions
-
- 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
- C10J2200/36—Moving parts inside the gasification reactor not otherwise provided for
-
- 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
Definitions
- the present invention relates to a composite gasification apparatus for coal gasification, and specifically, to a gasification furnace for sequentially performing fluidization, pyrolysis, and gasification by a circulating fluidized bed and a pyrolysis bed.
- the composite gasification apparatus is used for gasification of raw coal, and belongs to the field of coal gasification equipment technologies.
- the fixed bed gasifier has a high coal conversion rate and a high thermal efficiency, but the generated coal gas contains a large number of contaminants such as tar.
- the circulating fluidized bed gasifier can produce clean coal gas that does not contain contaminants such as tar, but it has low thermal efficiency of raw coal, coal slag contains a large amount of semi-coke, and coke-containing coal slag needs to be transported to a burning environment with low requirements for re-burning such as a raw material burnt in a thermal power plant.
- the coal utilization rate is decreased, and on the other hand, multiple items of costs such as transportation manpower are increased. Therefore, there is a need for a coal gasification device, which can ensure the high efficiency of converting raw coal into gas and obtain clean gas at the same time.
- US 4,552,078 discloses an apparatus and method for recycling fly ash to a fluidized bed coal gasifier.
- US 4,684,375 relates to a method and an installation for processing materials in a circulating fluidized bed, separating the solids from the produced gas and feeding them to a processing compartment before recycling them to the reactor.
- An objective of the present invention is to provide a method for implementing gasification by combining circulating fluidized bed and pyrolysis bed.
- combustion and gasification are performed by combining a circulating fluidized bed gasification furnace and a pyrolysis bed gasification furnace, thereby improving conversion efficiency of raw coal, and eliminating primary pollutants in coal gas.
- the objective of the present invention is further to provide an apparatus for implementing gasification by combining circulating fluidized bed and pyrolysis bed, which performs fluidized gasification and pyrolysis gasification on raw coal subsequently, and is a device configured to produce clean coal gas with the high conversion efficiency.
- the oblique guide plate is obliquely disposed in the deposition chamber.
- the gas distribution body is cone-shaped.
- a top portion of the central cylinder of the cyclone separator is in communication with the top portion of the deposition chamber by using the second coal gas pipe.
- the present invention provides a method for implementing gasification by combining circulating fluidized bed and pyrolysis bed.
- the method includes: combusting, fluidizing, and gasifying raw coal in an environment with a temperature of 900°C to 1200°C in a circulating fluidized bed gasification furnace preliminarily to generate coal gas, carbon-containing fly ash and semicoke, and feeding the carbon-containing fly ash and the semicoke into a cyclone separator together with the coal gas; introducing the coal gas, the carbon-containing fly ash, and the semicoke in the circulating fluidized bed gasification furnace into the cyclone separator from an upper portion of the cyclone separator, introducing separated semicoke into a pyrolysis bed gasification furnace, introducing a gasification agent into a bottom portion of the pyrolysis bed gasification furnace, and combusting the separated semicoke in the pyrolysis bed gasification furnace for further pyrolysis and gasification; introducing coal gas gas
- the gasification agent introduced into the bottom portion of the pyrolysis bed gasification furnace is mixed gases of air and vapor, and the semicoke are combusted and pyrolyzed in the pyrolysis bed gasification furnace.
- the gasification agent introduced into the bottom portion of the circulating fluidized bed gasification furnace is mixed gases of air, vapor and oxygen, and the raw coal are combusted and pyrolyzed in the circulating fluidized bed gasification furnace.
- the gasification agent introduced into the bottom portion of the pyrolysis bed gasification furnace is mixed gases of air, vapor and oxygen, and the semicoke are combusted and pyrolyzed in the pyrolysis bed gasification furnace.
- the apparatus further includes: a deposition chamber, a conveyor, a high-temperature air pipe, a vapor pipe, an oxygen pipe, and a fly ash pipe, where a top portion of the pyrolysis bed gasification furnace is in communication with a top portion of the deposition chamber by using a coal gas pipe; an oblique guide plate is disposed on an upper portion of the deposition chamber, and the conveyor is disposed on a bottom portion of the deposition chamber; and the conveyor is connected to the fly ash pipe; and the high-temperature air pipe, the vapor pipe, the oxygen pipe, and the fly ash pipe are in communication with the first mixture gas distribution chamber, and the high-temperature air pipe, the vapor pipe, and the oxygen pipe are in communication with the second mixture gas distribution chamber.
- the circulating fluidized bed gasification furnace has advantage of no pollutants, such as tar, during gasification
- the fixed gasification bed has advantage of high raw coal gasification rate
- the circulating fluidized bed gasification furnace and the pyrolysis bed gasification furnace are combined into one coal gasification device in the present invention, so that the combined coal gasification device not only does not produce pollutants such as tar, but also achieves high conversion rate of raw coal to gas.
- the present invention achieves a high raw coal gasification rate, produces no pollutants, such as tar, during gasification, is applicable to equipment with large, medium, and small gasification capacities, and has a large adjustment range of gas yield per unit time.
- FIG. 1 is a schematic structural diagram of an apparatus for implementing gasification by combining circulating fluidized bed and pyrolysis bed according to a first embodiment of the present invention.
- the apparatus includes a raw coal bunker 1, a circulating fluidized bed gasification furnace 2, a cyclone separator 3, a deposition chamber 4, a conveyor 5, a high-temperature air pipe 6, a vapor pipe 7, an oxygen pipe 8, a fly ash pipe 9, a slag pan 302 and a cone-shaped gas distribution body 301.
- the raw coal bunker 1 is in communication with the circulating fluidized bed gasification furnace 2 by using a coal conveying pipe.
- the coal gas, the carbon-containing fly ash C, and the semicoke B enter the cyclone separator 3 from an upper portion of the apparatus, and the semicoke B are further combusted, pyrolysed, and gasified in the pyrolysis bed gasification furnace.
- Coal gas generated in the pyrolysis bed gasification furnace, and the coal gas and the carbon-containing fly ash C that are generated in the circulating fluidized bed gasification furnace enter the deposition chamber 4 through the central cylinder of the cyclone separator 3, and coal slag are discharged from the slag pan 302 on the bottom portion of the pyrolysis bed gasification furnace.
- FIG. 2 is a schematic structural diagram of the apparatus for implementing gasification by combining circulating fluidized bed and pyrolysis bed according to an unclaimed embodiment not according to the invention.
- the apparatus includes a circulating fluidized bed gasification furnace 2 and a pyrolysis bed gasification furnace 11.
- the circulating fluidized bed gasification furnace 2 includes a coal conveying pipe 101 conveying raw coal to the circulating fluidized bed gasification furnace, and a gasification agent channel 102 introducing a gasification agent to a bottom portion of the circulating fluidized bed gasification furnace.
- the raw coal is fluidized bed combusted and pyrolysed in the circulating fluidized bed gasification furnace 2 to generate coal gas, carbon-containing fly ash and semicoke.
- An upper portion of the pyrolysis bed gasification furnace 11 is in communication with an upper portion of the circulating fluidized bed gasification furnace 2 by using a coal gas pipe.
- the oblique guide plate 114 can guide the coal gas, the carbon-containing fly ash and the semicoke that enter the pyrolysis bed gasification furnace 11 through the coal gas pipe to be downward, so that the semicoke drop onto the bottom portion of the pyrolysis bed gasification furnace 11 more easily.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Industrial Gases (AREA)
- Gasification And Melting Of Waste (AREA)
Claims (8)
- Vorrichtung zum Durchführen einer Vergasung von Rohkohle (A) durch Kombinieren eines zirkulierenden Wirbelbetts und eines Pyrolysebetts, aufweisend: einen Vergasungsofen mit zirkulierendem Wirbelbett (2), einen Zyklonabscheider (3), eine Abscheidungskammer (4), eine Fördereinrichtung (5), ein Hochtemperaturluftrohr (6), ein Sauerstoffrohr (8), ein Flugaschenrohr (9), eine Schlackenpfanne (302) und einen Vergasungsofen mit Pyrolysebett (301, 303) aufweisend einen Gasverteilungskörper (301), und
wobei die Rohkohle durch das Kohleförderrohr in den Vergasungsofen mit zirkulierendem Wirbelbett gelangt, ein oberer Abschnitt des Vergasungsofens mit zirkulierendem Wirbelbett über ein erstes Kohlegasrohr mit einem oberen Abschnitt des Zyklonabscheiders in Verbindung steht, und der Vergasungsofen mit zirkulierendem Wirbelbett eine Vergasungsofenkammer, welche an dessen oberem Abschnitt angeordnet ist, aufweist, dadurch gekennzeichnet, dass
die Vorrichtung auch ein Dampfrohr (7) aufweist, und ein oberer Abschnitt des Zyklonabscheiders über ein zweites Kohlegasrohr mit einem oberen Abschnitt der Abscheidungskammer in Verbindung steht;
wobei ein Gasverteiler (201) in einem mittleren Abschnitt des Vergasungsofens mit zirkulierendem Wirbelbett angeordnet ist, und eine erste Gasgemischverteilungskammer (202) an einem unteren Abschnitt desselben angeordnet ist; der Zyklonabscheider einen zentralen Zylinder angeordnet in einem Zentrum des oberen Abschnitts desselben aufweist, ein unterer Abschnitt des Zyklonabscheiders schwimmend an der Schlackenpfanne angeordnet ist, eine wasserdichte Abdichtung zwischen der Schlackenpfanne und dem unteren Abschnitt des Zyklonabscheiders angeordnet ist, der Gasverteilungskörper am unteren Abschnitt des Zyklonabscheiders und an der Schlackenpfanne angeordnet ist, eine zweite Gasgemischverteilungskammer (303) zwischen der Schlackenpfanne und einem unteren Abschnitt des Gasverteilungskörpers angeordnet ist; ein unterer Abschnitt eines inneren Hohlraums des Zyklonabscheiders, der Gasverteilungskörper und die zweite Gasgemischverteilungskammer unter dem Gasverteilungskörper zusammen den Vergasungsofen mit Pyrolysebett bilden; ein schräges Leitblech (401) an einem oberen Abschnitt der Abscheidungskammer angeordnet ist, und die Fördereinrichtung an einem unteren Abschnitt der Abscheidungskammer angeordnet und mit dem Flugaschenrohr verbunden ist; und
wobei das Hochtemperaturluftrohr, das Dampfrohr, das Sauerstoffrohr und das Flugaschenrohr mit der ersten Gasgemischverteilungskammer am unteren Abschnitt des Vergasungsofens mit zirkulierendem Wirbelbett in Verbindung stehen, und das Hochtemperaturluftrohr, das Dampfrohr und das Sauerstoffrohr mit der zweiten Gasgemischverteilungskammer angeordnet am unteren Abschnitt des Gasverteilungskörpers in Verbindung stehen. - Vorrichtung zum Durchführen einer Vergasung von Rohkohle (A) durch Kombinieren eines zirkulierenden Wirbelbetts und eines Pyrolysebetts nach Anspruch 1, wobei das schräge Leitblech in der Abscheidungskammer schräg angeordnet ist.
- Vorrichtung zum Durchführen einer Vergasung von Rohkohle (A) durch Kombinieren eines zirkulierenden Wirbelbetts und eines Pyrolysebetts nach Anspruch 1, wobei der Gasverteilungskörper kegelförmig ist.
- Vorrichtung zum Durchführen einer Vergasung von Rohkohle (A) durch Kombinieren eines zirkulierenden Wirbelbetts und eines Pyrolysebetts nach Anspruch 1, wobei ein oberer Abschnitt des zentralen Zylinders des Zyklonabscheiders über das zweite Kohlegasrohr mit dem oberen Abschnitt der Abscheidungskammer in Verbindung steht.
- Vergasungsverfahren zum Betreiben einer Vorrichtung nach Anspruch 1, umfassend:a. Verbrennen, Verwirbeln und Vergasen von Rohkohle (A) in einer Umgebung mit einer Temperatur von 900 °C bis 1200 °C in einem Vergasungsofen mit zirkulierendem Wirbelbett (2) vor dem Erzeugen von Kohlegas, kohlenstoffhaltiger Flugasche (C) und Schwelkoks (B), und Einspeisen der kohlenstoffhaltigen Flugasche und des Schwelkokses zusammen mit dem Kohlegas in einen Zyklonabscheider;b. Einleiten des Kohlegases, der kohlenstoffhaltigen Flugasche und des Schwelkokses im Vergasungsofen mit zirkulierendem Wirbelbett von einem oberen Abschnitt des Zyklonabscheiders in den Zyklonabscheider, Einleiten des abgeschiedenen Schwelkokses in einen Vergasungsofen mit Pyrolysebett (301, 303), Einleiten eines Vergasungsmittels in einen unteren Abschnitt des Vergasungsofen mit Pyrolysebett, und Verbrennen des abgeschiedenen Schwelkokses im Vergasungsofen mit Pyrolysebett zur weiteren Pyrolyse und Vergasung;c. Einleiten des im Vergasungsofen mit Pyrolysebett erzeugten Kohlegases, des im Vergasungsofen mit zirkulierendem Wirbelbett erzeugten Kohlegases und der im Vergasungsofen mit zirkulierendem Wirbelbett erzeugten kohlenstoffhaltigen Flugasche durch einen zentralen Zylinder des Zyklonabscheiders in eine Abscheidungskammer, und Austragen von Kohlenschlacke (D) aus einer Schlackenpfanne am unteren Abschnitt des Vergasungsofens mit Pyrolysebett; undd. Einleiten der in der Abscheidungskammer abgeschiedenen kohlenstoffhaltigen Flugasche in eine erste Gasgemischverteilungskammer an einem unteren Abschnitt des Vergasungsofens mit zirkulierendem Wirbelbett unter Verwendung einer Fördereinrichtung (5) und eines Flugaschenrohrs (9), und anschließendes Einleiten der zusammen mit einem Vergasungsmittel erhitzten kohlenstoffhaltigen Flugasche in den Vergasungsofen mit zirkulierendem Wirbelbett zur zirkulierenden Vergasung und Verbrennung.
- Verfahren nach Anspruch 5, wobei das in den unteren Abschnitt des Vergasungsofens mit Pyrolysebett eingeleitete Vergasungsmittel Gasgemisch aus Luft und Dampf ist, und der Schwelkoks im Vergasungsofen mit Pyrolysebett verbrannt und pyrolysiert wird.
- Verfahren nach Anspruch 5, wobei das in den unteren Abschnitt des Vergasungsofens mit zirkulierendem Wirbelbett eingeleitete Vergasungsmittel Gasgemisch aus Luft, Dampf und Sauerstoff ist, und die Rohkohle im Vergasungsofen mit zirkulierendem Wirbelbett verbrannt und pyrolysiert wird.
- Verfahren nach Anspruch 5, wobei das in den unteren Abschnitt des Vergasungsofens mit Pyrolysebett eingeleitete Vergasungsmittel Gasgemisch aus Luft, Dampf und Sauerstoff ist, und der Schwelkoks im Vergasungsofen mit Pyrolysebett verbrannt und pyrolysiert wird.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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CN201710048062.3A CN106635179B (zh) | 2017-01-23 | 2017-01-23 | 一种循环流化床与热解床复合气化的工艺及其装置 |
PCT/CN2017/088047 WO2018133303A1 (zh) | 2017-01-23 | 2017-06-13 | 一种循环流化床与热解床复合气化的方法及其装置 |
Publications (3)
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EP3540031A1 EP3540031A1 (de) | 2019-09-18 |
EP3540031A4 EP3540031A4 (de) | 2019-11-13 |
EP3540031B1 true EP3540031B1 (de) | 2021-03-03 |
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Country Status (5)
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US (1) | US20190367826A1 (de) |
EP (1) | EP3540031B1 (de) |
JP (1) | JP6716179B2 (de) |
CN (1) | CN106635179B (de) |
WO (1) | WO2018133303A1 (de) |
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CN106544059A (zh) * | 2017-01-22 | 2017-03-29 | 江苏华威机械制造有限公司 | 一种设置在旋风分离器下部的热解气化床 |
CN106635179B (zh) * | 2017-01-23 | 2019-03-08 | 江苏华威机械制造有限公司 | 一种循环流化床与热解床复合气化的工艺及其装置 |
CN107245344B (zh) * | 2017-06-24 | 2023-04-28 | 华中农业大学 | 农业废弃物低能耗的循环流化床炭化装置和方法 |
CN109355107B (zh) * | 2018-12-17 | 2023-08-22 | 江苏华威机械制造有限公司 | 一种煤制气复合气化装置 |
CN109852431B (zh) * | 2019-03-06 | 2020-11-06 | 中聚信海洋工程装备有限公司 | 一种循环流化双床热煤气站及其制气工艺 |
CN111925829A (zh) * | 2020-08-13 | 2020-11-13 | 刘建国 | 一种有机固废流化床-移动床两段式耦合气化装置 |
CN113528191B (zh) * | 2021-08-01 | 2022-12-02 | 中科聚信洁能热锻装备研发股份有限公司 | 一种精细分离焦渣的煤制气循环流化床 |
CN113583716B (zh) * | 2021-08-08 | 2023-07-14 | 中科聚信洁能热锻装备研发股份有限公司 | 一种双循环煤制气流化床 |
CN113583717B (zh) * | 2021-08-17 | 2023-07-18 | 中科聚信洁能热锻装备研发股份有限公司 | 一种沸腾燃烧与移动热解双炉复合的循环流化床 |
CN113684063A (zh) * | 2021-09-05 | 2021-11-23 | 中科聚信洁能热锻装备研发股份有限公司 | 一种燃尽含碳飞灰的双床复合煤气化炉 |
CN114106885B (zh) * | 2021-11-23 | 2022-07-26 | 新奥科技发展有限公司 | 气化炉***及其半焦分配控制方法 |
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CN101440308B (zh) * | 2008-12-23 | 2013-01-16 | 煤炭科学研究总院 | 一种固定床流化床串连式气化方法及装置 |
CN102212399B (zh) * | 2010-04-07 | 2014-01-29 | 中国科学院工程热物理研究所 | 热解气化联合方法及装置 |
CN103666567A (zh) * | 2012-09-20 | 2014-03-26 | 赵广健 | 一种沸腾式生物质气化*** |
FI126917B (fi) * | 2013-09-03 | 2017-08-15 | Valmet Technologies Oy | Järjestely ja menetelmä polttoaineen polttamiseksi |
CN103923704A (zh) * | 2014-04-16 | 2014-07-16 | 安徽科达洁能股份有限公司 | 煤气发生装置 |
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CN106635179B (zh) * | 2017-01-23 | 2019-03-08 | 江苏华威机械制造有限公司 | 一种循环流化床与热解床复合气化的工艺及其装置 |
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2017
- 2017-01-23 CN CN201710048062.3A patent/CN106635179B/zh active Active
- 2017-06-13 US US16/479,929 patent/US20190367826A1/en not_active Abandoned
- 2017-06-13 WO PCT/CN2017/088047 patent/WO2018133303A1/zh unknown
- 2017-06-13 JP JP2018556866A patent/JP6716179B2/ja not_active Expired - Fee Related
- 2017-06-13 EP EP17893195.2A patent/EP3540031B1/de active Active
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JP2019515996A (ja) | 2019-06-13 |
JP6716179B2 (ja) | 2020-07-01 |
US20190367826A1 (en) | 2019-12-05 |
CN106635179B (zh) | 2019-03-08 |
CN106635179A (zh) | 2017-05-10 |
EP3540031A1 (de) | 2019-09-18 |
EP3540031A4 (de) | 2019-11-13 |
WO2018133303A1 (zh) | 2018-07-26 |
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