WO2007101377A1 - A method for producing high-pressured and h2-enriched coal gas - Google Patents
A method for producing high-pressured and h2-enriched coal gas Download PDFInfo
- Publication number
- WO2007101377A1 WO2007101377A1 PCT/CN2006/003279 CN2006003279W WO2007101377A1 WO 2007101377 A1 WO2007101377 A1 WO 2007101377A1 CN 2006003279 W CN2006003279 W CN 2006003279W WO 2007101377 A1 WO2007101377 A1 WO 2007101377A1
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- WO
- WIPO (PCT)
- Prior art keywords
- gas
- pressure
- steam
- coal gas
- pressured
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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Classifications
-
- 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
-
- 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
- C10J3/463—Gasification of granular or pulverulent flues in suspension in stationary fluidised beds
-
- 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
- C10J3/725—Redox 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
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0973—Water
-
- 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
- C10J2300/1603—Integration of gasification processes with another plant or parts within the plant with gas treatment
- C10J2300/1609—Post-reduction, e.g. on a red-white-hot coke or coal bed
Definitions
- the present invention is directed to providing a process for the preparation of a high pressure, high hydrogen containing gas.
- the preparation method of high-pressure, high-hydrogen gas is to further pass the high-pressure steam obtained by the boiler
- a small amount of lime is added to the coke layer of the above shaft furnace to cause the sulfide to form calcium sulfide, which is removed with the slag.
- the invention has the following characteristics:
- the coal type has strong adaptability and can convert low quality coal into high quality gas.
- the water vapor and carbon dioxide content and nitrogen content in the gas are reduced to a very low level, and the gas heat value is high.
- the gas produced by this method has a high hydrogen content, and is particularly suitable for the development of hydrogen energy smelting and chemical synthesis gas and methanol.
- Figure 1 is a process flow diagram of the present invention.
- the high-pressure steam obtained by the boiler is further passed through a refractory heat storage device, and the steam is preheated to 100 (TC) under a pressure of 1.
- TC 100
- OMpa 100
- the high-volatility coal is subjected to dry distillation and gasification in a fluidized bed, and reaches the temperature at a temperature.
- it is sent to a shaft furnace filled with coke, and the gas is re-constructed twice. This gas is directly used by the user after dust removal and purification.
- the appropriate pure oxygen is added to adjust the gas production and Gas composition, oxygen pressure is greater than steam pressure.
- the high-pressure steam obtained by Jiang from the boiler is further preheated to 120 (TC, under the pressure of 1.2 Mpa) through the refractory heat storage and heat exchange device, and the high-volatility coal is retorted and gasified by the fluidized bed, 'and When the temperature reaches 120 (TC), it is sent to the shaft furnace filled with coke, and the secondary reforming and re-construction gas is used.
- the coal is directly used by the user after dust removal and purification. Before the hot dirty gas is sent to the shaft furnace, it is added. Appropriate pure oxygen adjusts gas production and gas composition, and oxygen pressure is greater than steam pressure.
- the high-pressure steam obtained by the boiler is further heated by a refractory material, and the steam is preheated to 1300 ° C under a pressure of 1.5 Mpa, and the high-volatility coal is dried by a fluidized bed at a temperature of 1300 °.
- it is sent to the shaft furnace filled with coke,: : Secondary reforming #3 ⁇ 4 gas, this gas is directly used by users after dust removal and purification.
- the appropriate pure oxygen is added to adjust the gas production and gas composition, and the oxygen pressure is greater than the steam pressure.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Industrial Gases (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
高压、 高含氢煤气的制备方法 技术领域: Preparation method of high pressure and high hydrogen containing gas Technical field:
:' ;:'·本^:明 及一种煤气制备方法,具体为一种高压、 :高含氢煤气的制备 方法。 : ';:' * ^ Present: A process for preparing clear and gas, in particular to a high pressure: preparation of high hydrogen gas.
'技 背景: 'Technical background:
; ..'·在冶金 »化工合成工业中洁净煤综合利用, 煤的气化和生产高热值、 高含氢煤气在上述工业中有着广阔的用途, 也是难以解决的高难课题之 发明内容: ; .. '·In the metallurgy»Chemical synthesis industry, the comprehensive utilization of clean coal, coal gasification and production of high calorific value, high hydrogen gas in the above-mentioned industries have a wide range of uses, is also difficult to solve the difficult problem of the invention:
' ·本发明 ¾目的在于提供一种高压、 高含氢煤气的制备方法。 The present invention is directed to providing a process for the preparation of a high pressure, high hydrogen containing gas.
采用的技术方案是: The technical solution adopted is:
高压、高含氢煤气的制备方法, 是将由锅炉得到的高压蒸汽进一步通 The preparation method of high-pressure, high-hydrogen gas is to further pass the high-pressure steam obtained by the boiler
..过耐火材料蓄热, 由换热装置蒸汽在 0. 1—3. OMpa压力下预热到 90CTC— 1300°C , 再利用流化床将高挥发份的煤进行干馏和气化, 在温度达到 900 : C以上时, 送至装满焦碳的竖炉, 二次重整再造煤气, 此煤气经除尘净化 .后,:直接供用户使用。 .. through the refractory heat storage, preheated from the heat exchanger steam at 0. 1 - 3. OMpa pressure to 90CTC - 1300 ° C, and then use the fluidized bed to dry distillation and gasification of high volatile coal, at temperature after C or higher, to the shaft furnace filled with coke, the secondary reformed gas recycling, this dust through gas purification:: 900. directly available to users.
上述的热脏煤气送入竖炉之前,可加入适当纯氧调整煤气产量和煤气 成份 氧气压力应大于蒸汽压力。 Before the above hot dirty gas is sent to the shaft furnace, appropriate pure oxygen can be added to adjust the gas production and gas composition. The oxygen pressure should be greater than the steam pressure.
上述的竖炉的焦碳层中加入少量石灰,使硫化物生成硫化钙, 随炉渣 排除。 :':; : 本发明具有如下特点: A small amount of lime is added to the coke layer of the above shaft furnace to cause the sulfide to form calcium sulfide, which is removed with the slag. :': ; : The invention has the following characteristics:
. 1、 煤种适应性强, 可以使劣质煤也通过转换成优质煤气。 1. The coal type has strong adaptability and can convert low quality coal into high quality gas.
2、 使煤气中水蒸汽和二氧化碳含量、 氮气含量降至很低, 煤气热值 高。 2. The water vapor and carbon dioxide content and nitrogen content in the gas are reduced to a very low level, and the gas heat value is high.
¾^'3、 全过程都在蒸汽压力下进行, 因此获得高压煤气不需要压缩机压 缩,.减少二次能源消耗。 3⁄4^'3, the whole process is carried out under steam pressure, so the high pressure gas does not require compressor compression, reducing secondary energy consumption.
4、 此方法制备的煤气含氢量高, 尤其适合发展氢能源冶炼和化工合 成气和甲醇。 4. The gas produced by this method has a high hydrogen content, and is particularly suitable for the development of hydrogen energy smelting and chemical synthesis gas and methanol.
附图说明: BRIEF DESCRIPTION OF THE DRAWINGS:
图 1为本发明的工艺流程图。 Figure 1 is a process flow diagram of the present invention.
具体实施方式: detailed description:
实施例一 Embodiment 1
将由锅炉得到的高压蒸汽进一步通过耐火材料蓄热、换热装置将蒸汽 在 1. OMpa压力下预热到 100(TC, 用流化床将高挥发份的煤进行干馏和气 化, 并在温度达到 1000Ό时, 送至装满焦碳的竖炉, 二次重整再造煤气, 此煤气经除尘净化后, 直接供用户使用。在热脏煤气送入竖炉之前, 加入 适当纯氧调整煤气产量和煤气成份, 氧气压力大于蒸汽压力。 The high-pressure steam obtained by the boiler is further passed through a refractory heat storage device, and the steam is preheated to 100 (TC) under a pressure of 1. OMpa, and the high-volatility coal is subjected to dry distillation and gasification in a fluidized bed, and reaches the temperature at a temperature. At 1000 ,, it is sent to a shaft furnace filled with coke, and the gas is re-constructed twice. This gas is directly used by the user after dust removal and purification. Before the hot dirty gas is sent to the shaft furnace, the appropriate pure oxygen is added to adjust the gas production and Gas composition, oxygen pressure is greater than steam pressure.
. .实施例二 .Example 2
蒋由锅炉得到的高压蒸汽进一步通过耐火材料蓄热、换热装置将蒸汽 •在 1. 2Mpa压力下预热到 120(TC, 用流化床将高挥发份的煤进行干馏和气 化,'并在温度达到 120(TC时, 送至装满焦碳的竖炉, 二次重整再造煤气, 此煤 经除尘净化后, 直接供用户使用。在热脏煤气送入竖炉之前, 加入 适当纯氧调整煤气产量和煤气成份, 氧气压力大于蒸汽压力。 The high-pressure steam obtained by Jiang from the boiler is further preheated to 120 (TC, under the pressure of 1.2 Mpa) through the refractory heat storage and heat exchange device, and the high-volatility coal is retorted and gasified by the fluidized bed, 'and When the temperature reaches 120 (TC), it is sent to the shaft furnace filled with coke, and the secondary reforming and re-construction gas is used. The coal is directly used by the user after dust removal and purification. Before the hot dirty gas is sent to the shaft furnace, it is added. Appropriate pure oxygen adjusts gas production and gas composition, and oxygen pressure is greater than steam pressure.
•实施例三 •Example 3
将由锅炉得到的高压蒸汽进一步通过耐火材料蓄热、换热装置将蒸汽 在 1. 5Mpa压力下预热到 1300°C, 用流化床将高挥发份的煤进行干熘和气 在温度达到 1300°C时, 送至装满焦碳的竖炉,: :二次重整#¾煤气, 此煤气经除尘净化后, 直接供用户使用。在热脏煤气送入竖炉之前, 加入 适当纯氧调整煤气产量和煤气成份, 氧气压力大于蒸汽压力。 The high-pressure steam obtained by the boiler is further heated by a refractory material, and the steam is preheated to 1300 ° C under a pressure of 1.5 Mpa, and the high-volatility coal is dried by a fluidized bed at a temperature of 1300 °. At time C, it is sent to the shaft furnace filled with coke,: : Secondary reforming #3⁄4 gas, this gas is directly used by users after dust removal and purification. Before the hot dirty gas is sent to the shaft furnace, the appropriate pure oxygen is added to adjust the gas production and gas composition, and the oxygen pressure is greater than the steam pressure.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610045968 CN1818032A (en) | 2006-03-06 | 2006-03-06 | Production of high-hydrogen content gas with high pressure |
| CN200610045968.1 | 2006-03-06 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2007101377A1 true WO2007101377A1 (en) | 2007-09-13 |
Family
ID=36918236
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2006/003279 Ceased WO2007101377A1 (en) | 2006-03-06 | 2006-12-05 | A method for producing high-pressured and h2-enriched coal gas |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN1818032A (en) |
| WO (1) | WO2007101377A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009050494A3 (en) * | 2007-10-20 | 2009-09-11 | Moulson Process Plant Limited | Production of fuel from refuse |
| US8500868B2 (en) | 2009-05-01 | 2013-08-06 | Massachusetts Institute Of Technology | Systems and methods for the separation of carbon dioxide and water |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010514858A (en) * | 2006-12-28 | 2010-05-06 | ゾウ,ジウレ | Pulverized coal gas stove |
| CN101210201B (en) * | 2006-12-30 | 2010-09-22 | 沈阳东方钢铁有限公司 | A dry pulverized coal gasifier |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2705672A (en) * | 1953-07-20 | 1955-04-05 | Consolidation Coal Co | Manufacture of water gas |
| US4004896A (en) * | 1974-11-21 | 1977-01-25 | University Of Illinois Foundation | Production of water gas |
| US4397656A (en) * | 1982-02-01 | 1983-08-09 | Mobil Oil Corporation | Process for the combined coking and gasification of coal |
| CN85109363A (en) * | 1984-12-28 | 1986-06-10 | Skf钢铁工程有限公司 | System gas |
| CN86104143A (en) * | 1986-12-26 | 1988-07-13 | 华东化工学院 | A kind of method of manufacturing synthesis gas from new born coal |
| US4876080A (en) * | 1986-12-12 | 1989-10-24 | The United States Of Americal As Represented By The United States Department Of Energy | Hydrogen production with coal using a pulverization device |
| JPH04213688A (en) * | 1990-02-02 | 1992-08-04 | Nergeco Sa | Roller curtain type door for take-in and take-out of goods |
-
2006
- 2006-03-06 CN CN 200610045968 patent/CN1818032A/en active Pending
- 2006-12-05 WO PCT/CN2006/003279 patent/WO2007101377A1/en not_active Ceased
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2705672A (en) * | 1953-07-20 | 1955-04-05 | Consolidation Coal Co | Manufacture of water gas |
| US4004896A (en) * | 1974-11-21 | 1977-01-25 | University Of Illinois Foundation | Production of water gas |
| US4397656A (en) * | 1982-02-01 | 1983-08-09 | Mobil Oil Corporation | Process for the combined coking and gasification of coal |
| CN85109363A (en) * | 1984-12-28 | 1986-06-10 | Skf钢铁工程有限公司 | System gas |
| US4876080A (en) * | 1986-12-12 | 1989-10-24 | The United States Of Americal As Represented By The United States Department Of Energy | Hydrogen production with coal using a pulverization device |
| CN86104143A (en) * | 1986-12-26 | 1988-07-13 | 华东化工学院 | A kind of method of manufacturing synthesis gas from new born coal |
| JPH04213688A (en) * | 1990-02-02 | 1992-08-04 | Nergeco Sa | Roller curtain type door for take-in and take-out of goods |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009050494A3 (en) * | 2007-10-20 | 2009-09-11 | Moulson Process Plant Limited | Production of fuel from refuse |
| US8500868B2 (en) | 2009-05-01 | 2013-08-06 | Massachusetts Institute Of Technology | Systems and methods for the separation of carbon dioxide and water |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1818032A (en) | 2006-08-16 |
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