WO2009153948A1 - ガス化ガスの改質方法及び装置 - Google Patents
ガス化ガスの改質方法及び装置 Download PDFInfo
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- WO2009153948A1 WO2009153948A1 PCT/JP2009/002661 JP2009002661W WO2009153948A1 WO 2009153948 A1 WO2009153948 A1 WO 2009153948A1 JP 2009002661 W JP2009002661 W JP 2009002661W WO 2009153948 A1 WO2009153948 A1 WO 2009153948A1
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- Prior art keywords
- reforming
- gasification gas
- stage
- furnace
- oxygen
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
- C10K3/001—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by thermal treatment
- C10K3/003—Reducing the tar content
- C10K3/005—Reducing the tar content by partial oxidation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
- B01J4/002—Nozzle-type elements
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
- C10K3/001—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by thermal treatment
- C10K3/003—Reducing the tar content
- C10K3/008—Reducing the tar content by cracking
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
- B01J2204/002—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the feeding side being of particular interest
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00164—Controlling or regulating processes controlling the flow
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0211—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step
- C01B2203/0216—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step containing a non-catalytic steam reforming step
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
Definitions
- the present invention relates to a gasification gas reforming method and apparatus capable of enhancing the production of hydrogen by a simple apparatus.
- raw materials such as coal and biomass have been gasified by a gasification apparatus such as a fluidized bed gasification furnace or a fixed bed gasification furnace to generate a highly combustible gasification gas.
- a gasification apparatus such as a fluidized bed gasification furnace or a fixed bed gasification furnace to generate a highly combustible gasification gas.
- the gasification gas contains water vapor (H 2 O) and tar together with gas components such as hydrogen (H 2 ), hydrocarbon (C m H n ), carbon monoxide (CO), and carbon dioxide (CO 2 ). is doing.
- the gasified gas generated by the gasifier is used after being transported to the subsequent purification or other various equipment as described above. At this time, the tar contained in the gasified gas is used for piping and equipment. In the past, scrubbers were installed and tar was removed by water injection.
- the gasified gas is supplied to the reforming furnace, and oxygen (O 2 ) is supplied to burn a part of the gasified gas to raise the temperature to reform the tar.
- oxygen (O 2 ) is supplied to burn a part of the gasified gas to raise the temperature to reform the tar.
- the unmodified tar becomes solid carbon (char), thereby preventing the problem of adhesion and deposition on the piping and equipment.
- the reformed gas is composed of H 2, CO, and CH. It will be enriched.
- the hydrocarbon is reformed by the following reaction.
- the product of the reforming reaction reacts as follows by supplying oxygen (O 2 ).
- Patent Document 1 and Patent Document 2 are prior art information that has been disclosed about the reforming furnace.
- gasification gas and oxygen are supplied from one end of the reforming furnace, and a part of the gasification gas is burned with oxygen for reforming.
- Gasification gas reforming is performed by raising the inside of the furnace to the reforming target temperature at which reforming proceeds and maintaining the reforming target temperature for a required time (maintaining the reaction time).
- the present invention has been made in view of the above circumstances, and an object of the present invention is to provide a gasification gas reforming method and apparatus capable of enhancing the production of hydrogen by a small and simple apparatus.
- the present invention provides gasification by supplying a gasification gas containing tar and oxygen to a reforming furnace and partially combusting the gasification gas to raise the inside of the reforming furnace to a reforming target temperature required for reforming.
- a gasification gas reforming method for reforming gas wherein oxygen and first stage gasification gas are modified in such an amount that the gasification gas is combusted by oxygen to obtain a reforming target temperature required for reforming.
- a heating zone is formed in the reforming furnace by supplying from one end of the quality furnace, and the remaining gasification gas is supplied as a second stage gasification gas near the downstream of the heating zone in the reforming furnace.
- the present invention relates to a gasification gas reforming method characterized by forming a mass region.
- the target reforming temperature in the reforming zone is preferably 900 to 1400 ° C.
- the heating temperature in the heating zone high in consideration of the temperature decrease in which the temperature in the reforming zone is lowered by the supply of the second stage gasification gas.
- the oxygen supply path has a flow rate adjusting means for adjusting the amount of oxygen supplied to the reforming furnace through the oxygen supply path.
- the flow rate adjustment for adjusting the supply amount of the gasification gas supplied to the reforming furnace through the first-stage gasification gas supply passage in the first-stage gasification gas supply passage is preferable to have a means.
- the first-stage gasification gas supply path has a first-stage nozzle that supplies gasification gas from the tangential direction to the outer peripheral wall of the reforming furnace.
- a plurality of first stage nozzles are arranged at equal intervals in the circumferential direction of the reforming furnace.
- a plurality of second stage nozzles are arranged at equal intervals in the circumferential direction of the reforming furnace.
- oxygen and the first stage gasification gas are modified in such an amount that the gasification gas is combusted by oxygen to obtain a reforming target temperature necessary for reforming.
- a heating zone is formed in the reforming furnace by supplying from one end of the quality furnace, and the remaining gasification gas is supplied as a second stage gasification gas near the downstream of the heating zone in the reforming furnace.
- FIG. 1 is an oblique front view showing an embodiment of the reformer of the present invention
- FIG. 2 is a plan view of the reformer of FIG.
- reference numeral 1 denotes a reforming furnace having a cylindrical shape.
- One end of the reforming furnace 1 (upper end in FIG. 1) is a part of the gasified gas 3 generated by the gasifier 2.
- a first-stage gasification gas supply path 4 that supplies the first-stage gasification gas 3a is provided.
- the first-stage gasification gas supply path 4 has a first-stage nozzle 5 for supplying the first-stage gasification gas 3a from the tangential direction to the outer peripheral wall on one end side of the reforming furnace 1.
- a swirl flow is formed in the quality furnace 1.
- a second stage in which the remainder of the gasification gas 3 from the gasifier 2 is branched and supplied as a second stage gasification gas 3b to an intermediate portion separated from the one end of the reforming furnace 1.
- a gasification gas supply path 6 is provided.
- the second-stage gasification gas supply path 6 has a second-stage nozzle 7 for supplying the second-stage gasification gas 3b from the tangential direction to the outer peripheral wall of the reforming furnace 1, and the reforming furnace 1 A swirling flow in the same direction as the first stage nozzle 5 is formed inside.
- the first-stage gasification gas supply path 4 includes a valve for adjusting the supply amount of the first-stage gasification gas 3a supplied to the reforming furnace 1 by the first-stage gasification gas supply path 4.
- a flow rate adjusting means 8 is provided.
- An oxygen supply path 10 for supplying oxygen 9 (O 2 ) is provided on one end face of the reforming furnace 1, and the oxygen supply path 10 includes a plurality (four in FIG. 2) of oxygen nozzles 11.
- the plurality of oxygen nozzles 11 are connected to the reforming furnace 1 to improve the mixing of oxygen 9 with the first stage gasification gas 3a supplied from the first stage nozzle 5.
- the oxygen supply passage 10 is provided with a flow rate adjusting means 12 for adjusting the supply amount of oxygen 9 supplied to the reforming furnace 1 through the oxygen supply passage 10.
- the oxygen supply path 10 is connected to the first stage nozzle 5 as shown by a broken line in FIG. You may make it do.
- the flow rate adjusting means 12 supplies oxygen 9 in an amount capable of obtaining a reforming target temperature (900 to 1400 ° C.) required for reforming in the reforming furnace 1 from the oxygen supply path 10 by combustion with the gasified gas 3.
- the first stage gasification gas 3 a is supplied from the first stage gasification gas supply passage 4 by the flow rate adjusting means 8 in such an amount that the reforming target temperature can be obtained by combustion with the oxygen 9.
- a heating zone A is formed inside one end side of the reforming furnace 1.
- the second-stage gasification gas supply path 6 is connected to the reforming furnace 1 at a position directly below the end point X downstream of the heating zone A, so that from the end point X of the heating zone A, A reforming zone B is formed between the other ends (lower ends) of the reforming furnace 1, and a reforming target temperature of 900 to 1400 ° C. is maintained in the reforming zone B.
- the connection position of the second stage gasification gas supply path 6 with respect to the reforming furnace 1 may be in the vicinity of the downstream of the heating zone A, but reforming when connected to a position immediately below the end point X of the heating zone A. Since the furnace 1 can be reduced in size, it is preferable.
- the temperature of the reforming zone B Since the temperature of the reforming zone B is also lowered by the endothermic reaction at this time, the temperature of the reforming zone B becomes, for example, 1100 ° C., and the temperature required for reforming may not be obtained. For this reason, the temperature of the heating zone A is set to a high temperature that allows for the temperature drop in the reforming zone B based on calorie calculation or empirical rules. That is, by adjusting the supply amount of the first stage gasification gas 3a by the flow rate adjusting means 8 and the supply amount of oxygen 9 by the flow rate adjusting means 12 so as to maintain the temperature of the heating zone A at, for example, 1400 ° C. The reforming target temperature 1200 ° C. of the mass region B is maintained.
- a take-out flow path 14 for taking out the gas 13 after reforming, and the take-out flow path 14 has an outer periphery of the reforming furnace 1 so as to hold the swirl flow. Connected tangential to the wall.
- a part of the gasified gas 3 generated by the gasifier 2 is formed as a first-stage gasified gas 3a at one end of the reforming furnace 1 via the first-stage gasified gas supply path 4 and the first-stage nozzle 5.
- the intermediate part which is supplied tangentially and the remaining gasification gas 3 is separated from one end of the reforming furnace 1 through the second stage nozzle 7 by the second stage gasification gas supply path 6 as the second stage gasification gas 3b. Is tangentially supplied.
- oxygen 9 from the oxygen supply path 10 is supplied into the reforming furnace 1 through an oxygen nozzle 11 provided at one end face of the reforming furnace 1.
- a flow rate of oxygen 9 from the oxygen supply passage 10 is obtained in the reforming furnace 1 so as to obtain a reforming target temperature of, for example, 900 to 1400 ° C. necessary for reforming by combustion with the first stage gasified gas 3a.
- the first stage gasification gas 3a is supplied from the first stage gasification gas supply passage 4 through the first stage gasification gas supply passage 4 by the flow rate adjustment means 8 in such an amount that the reforming target temperature can be obtained by combustion with the oxygen 9.
- a heating zone A is formed inside one end of the reforming furnace 1 as shown in FIG. At this time, the heating temperature of the heating zone A is set to a high temperature in anticipation of a temperature drop in which the temperature of the reforming zone B decreases due to the supply of the second stage gasification gas.
- H 2 in the first stage gasification gas 3a is first selectively burned to raise the temperature, and then CO and CH in the first stage gasification gas 3a are burned. By further raising the temperature, tar in the first stage gasification gas 3a is also combusted.
- the oxygen 9 supplied from the oxygen supply path 10 is burned out.
- the second-stage gasification gas 3b by the second-stage gasification gas supply path 6 is supplied immediately below the end point X of the heating area A, the second-stage gasification gas 3b is second in the reforming area B where oxygen is burned out. H 2 in the staged gasification gas 3b does not burn, and only the reforming reaction is promoted in the reforming zone B. Therefore, the reformed gas 13 with increased concentrations of H 2, CO, and CH is taken out from the take-out flow path 14.
- the reformed target temperature at which reforming proceeds downstream is maintained by supplying a set amount of the first-stage gasification gas 3a and oxygen 9 to one end of the reforming furnace 1 and burning them.
- the heating zone A is formed so as to form the reforming zone B, and the second stage gasification gas 3b is supplied to the reforming zone B formed immediately below the end point X downstream of the heating zone A for reforming.
- tar in the first stage gasification gas 3a is also combusted and supplied immediately below the end point X downstream of the heating zone A.
- the second stage gasification gas 3b only the reforming reaction is promoted without burning H 2 in the reforming zone B maintained at the reforming target temperature with the oxygen 9 burned out. Therefore, the modified gas 13 with an increased H 2 concentration can be obtained.
- the reaction time can be shortened compared to the conventional case,
- the furnace 1 can be reduced in size.
- the first-stage gasification gas supply path 4 has an annular supply pipe 15 surrounding the reforming furnace 1.
- a plurality of first stage nozzles 5a configured to supply the first stage gasification gas 3a in a tangential direction to the reforming furnace 1 are provided at equal circumferential positions in the annular supply pipe 15. It is arranged.
- the second-stage supply gasification gas passage 6 also has an annular supply pipe 16 surrounding the reforming furnace 1, and the annular supply pipe 16 has a circumferentially equidistant position with respect to the reforming furnace 1.
- a plurality of second stage nozzles 7a are arranged so as to supply the second stage gasification gas 3b in the tangential direction.
- the first stage gasification is performed.
- the gas 3a and the second-stage gasification gas 3b are distributedly supplied into the reforming furnace 1, so that uniform heating in the heating zone A and uniform reforming reaction in the reforming zone B are performed. be able to.
- this invention is not limited only to the said Example, Of course, a various change can be added in the range which does not deviate from the summary of this invention.
- the gasification gas reforming method and apparatus of the present invention can be applied when the reforming reaction is effectively promoted to downsize the reforming furnace.
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Abstract
Description
3 ガス化ガス
3a 第1段ガス化ガス
3b 第2段ガス化ガス
4 第1段ガス化ガス供給路
5 第1段ノズル
5a 第1段ノズル
6 第2段ガス化ガス供給路
7 第2段ノズル
7a 第2段ノズル
8 流量調節手段
9 酸素
10 酸素供給路
12 流量調節手段
A 加熱域
B 改質域
X 終了点
Claims (14)
- タールを含有するガス化ガスと酸素とを改質炉に供給し、ガス化ガスを部分燃焼させて改質炉内を改質に必要な改質目標温度に高めることによりガス化ガスの改質を行うガス化ガスの改質方法であって、酸素によりガス化ガスが燃焼して改質に必要な改質目標温度が得られる量の酸素及び第1段ガス化ガスを改質炉の一端側から供給することにより改質炉内に加熱域を形成し、改質炉内における加熱域の下流近傍に残りのガス化ガスを第2段ガス化ガスとして供給することにより改質域を形成することを特徴とするガス化ガスの改質方法。
- 改質域での改質目標温度が900~1400℃であることを特徴とする請求項1に記載のガス化ガスの改質方法。
- 第2段ガス化ガスの供給により改質域の温度が低下する温度低下分を見込んで加熱域での加熱温度を高く設定することを特徴とする請求項1又は2に記載のガス化ガスの改質方法。
- タールを含有するガス化ガスと酸素とを改質炉に供給し、ガス化ガスを部分燃焼させて改質炉内を改質に必要な改質目標温度に高めることによりガス化ガスの改質を行うガス化ガスの改質装置であって、酸素によりガス化ガスが燃焼して改質に必要な改質目標温度が得られる量の酸素とガス化ガスの一部とを改質炉の一端から供給して改質炉内に加熱域を形成するための酸素供給路及び第1段ガス化ガス供給路と、前記加熱域の下流近傍に残りのガス化ガスを供給して改質域を形成する第2段ガス化ガス供給路と、を有することを特徴とするガス化ガスの改質装置。
- 酸素供給路は、該酸素供給路によって改質炉に供給する酸素の供給量を調節するための流量調節手段を有することを特徴とする請求項4に記載のガス化ガスの改質装置。
- 第1段ガス化ガス供給路は、該第1段ガス化ガス供給路によって改質炉に供給するガス化ガスの供給量を調節するための流量調節手段を有することを特徴とする請求項4に記載のガス化ガスの改質装置。
- 第1段ガス化ガス供給路は、該第1段ガス化ガス供給路によって改質炉に供給するガス化ガスの供給量を調節するための流量調節手段を有することを特徴とする請求項5に記載のガス化ガスの改質装置。
- 第1段ガス化ガス供給路は、改質炉の外周壁に接線方向からガス化ガスを供給する第1段ノズルを有していることを特徴とする請求項6に記載のガス化ガスの改質装置。
- 第1段ガス化ガス供給路は、改質炉の外周壁に接線方向からガス化ガスを供給する第1段ノズルを有していることを特徴とする請求項7に記載のガス化ガスの改質装置。
- 第1段ノズルは、改質炉の周方向に等間隔で複数配置されていることを特徴とする請求項8又は9に記載のガス化ガスの改質装置。
- 第2段ガス化ガス供給路は、改質炉の外周壁に対して接線方向からガス化ガスを供給する第2段ノズルを有することを特徴とする請求項4に記載のガス化ガスの改質装置。
- 第2段ガス化ガス供給路は、改質炉の外周壁に対して接線方向からガス化ガスを供給する第2段ノズルを有することを特徴とする請求項8に記載のガス化ガスの改質装置。
- 第2段ガス化ガス供給路は、改質炉の外周壁に対して接線方向からガス化ガスを供給する第2段ノズルを有することを特徴とする請求項9に記載のガス化ガスの改質装置。
- 第2段ノズルは、改質炉の周方向に等間隔で複数配置されていることを特徴とする請求項11、12又は13に記載のガス化ガスの改質装置。
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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US12/995,328 US8741179B2 (en) | 2008-06-17 | 2009-06-12 | Process and equipment for reforming gasification gas |
AU2009261429A AU2009261429B2 (en) | 2008-06-17 | 2009-06-12 | Process and equipment for reforming gasification gas |
CN2009801233720A CN102066532B (zh) | 2008-06-17 | 2009-06-12 | 气化气体的重整方法及装置 |
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JP2008-157382 | 2008-06-17 | ||
JP2008157382A JP5282455B2 (ja) | 2008-06-17 | 2008-06-17 | ガス化ガスの改質方法及び装置 |
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PCT/JP2009/002661 WO2009153948A1 (ja) | 2008-06-17 | 2009-06-12 | ガス化ガスの改質方法及び装置 |
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US (1) | US8741179B2 (ja) |
JP (1) | JP5282455B2 (ja) |
CN (1) | CN102066532B (ja) |
AU (1) | AU2009261429B2 (ja) |
WO (1) | WO2009153948A1 (ja) |
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US20120255301A1 (en) * | 2011-04-06 | 2012-10-11 | Bell Peter S | System for generating power from a syngas fermentation process |
JP6248495B2 (ja) * | 2013-09-18 | 2017-12-20 | 株式会社Ihi | ガス化ガス中のタールの改質装置 |
JP6229526B2 (ja) * | 2014-02-13 | 2017-11-15 | 株式会社Ihi | タール改質炉及びそのガス化設備 |
GB2551314B (en) * | 2016-06-06 | 2021-03-17 | Kew Tech Limited | Equilibium approach reactor |
JP6693345B2 (ja) * | 2016-08-31 | 2020-05-13 | 株式会社Ihi | タール改質装置 |
JP6822025B2 (ja) * | 2016-09-12 | 2021-01-27 | 株式会社Ihi | タール改質装置 |
CN110964572B (zh) * | 2019-12-12 | 2021-08-20 | 郑州轻工业大学 | 一种防止炉壁烧损的气化剂切圆强旋转煤粉气化炉装置 |
GB2595004B (en) * | 2020-05-13 | 2023-05-17 | Velocys Tech Limited | Production of synthetic fuels |
CN112852494A (zh) * | 2020-12-24 | 2021-05-28 | 中广核研究院有限公司 | 分布式固体废弃物气化熔融发电***及其方法 |
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US20110076227A1 (en) | 2011-03-31 |
CN102066532B (zh) | 2013-09-25 |
AU2009261429B2 (en) | 2013-05-23 |
US8741179B2 (en) | 2014-06-03 |
AU2009261429A1 (en) | 2009-12-23 |
CN102066532A (zh) | 2011-05-18 |
JP5282455B2 (ja) | 2013-09-04 |
JP2009298974A (ja) | 2009-12-24 |
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