WO2012048515A1 - 复合粉煤气化方法 - Google Patents

复合粉煤气化方法 Download PDF

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Publication number
WO2012048515A1
WO2012048515A1 PCT/CN2011/001193 CN2011001193W WO2012048515A1 WO 2012048515 A1 WO2012048515 A1 WO 2012048515A1 CN 2011001193 W CN2011001193 W CN 2011001193W WO 2012048515 A1 WO2012048515 A1 WO 2012048515A1
Authority
WO
WIPO (PCT)
Prior art keywords
coal
coal gasification
gasification
slag
gasification system
Prior art date
Application number
PCT/CN2011/001193
Other languages
English (en)
French (fr)
Inventor
邰学林
Original Assignee
Tai Xuelin
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tai Xuelin filed Critical Tai Xuelin
Publication of WO2012048515A1 publication Critical patent/WO2012048515A1/zh

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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
    • C10J3/48—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
    • C10J3/72—Other features
    • C10J3/721—Multistage gasification, e.g. plural parallel or serial gasification stages
    • 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
    • C10J2300/0903—Feed preparation
    • C10J2300/0906—Physical processes, e.g. shredding, comminuting, chopping, sorting
    • 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
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/093—Coal
    • 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
    • C10J2300/0956—Air or oxygen enriched air
    • 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
    • C10J2300/0959—Oxygen
    • 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
    • C10J2300/0969—Carbon dioxide
    • 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
    • C10J2300/0976—Water as steam

Definitions

  • the invention relates to the field of coal chemical industry.
  • the present invention refers to the simultaneous use of fluidized bed gasification technology and slag entrained flow gasification technology in a powder coal gasification system.
  • the invention adopts the fluidized bed gasification furnace and the slag flow bed gasification furnace series technology, the common way to enter the coal, the pulverized coal in the fluidization
  • the primary gasification in the bed gasifier enters the slag entrained gasifier and further vaporizes the high temperature slag.
  • the liquid slag naturally flows from the lower part of the gasifier into the slag cold discharge system.
  • the high temperature reaction gas is cooled or cooled. After the water is cooled and cooled, it leaves the gasifier.
  • the raw coal feed is simple, no special raw coal treatment, transportation system, special powder coal gasification nozzle are needed, and gas and slag separation is simple. This reduces the complexity of the coal gasification system and reduces the energy consumption, manufacturing and operating costs of the coal gasification system.
  • FIG. 1 is a schematic diagram of the present invention.
  • the initially crushed pulverized coal enters the fluidized bed 3 from the coal conveyor 2, the gasifying agent oxygen, or a mixture of oxygen and water vapor, or a mixture of oxygen and carbon dioxide is sent to the fluidized bed through the gasifying agent inlet nozzle 1 3.
  • the crude gas containing fine coal powder enters the slag gas flow bed 5 through the outlet pipe 4 of the fluidized bed 3, and oxygen or oxygen added through the gasification agent nozzle 7.
  • the high-temperature gasification reaction is carried out together with steam, or a mixture of oxygen and carbon dioxide, and the molten slag after the reaction naturally flows into the slag discharge system 6 through the lower portion of the slag flow bed 5, and is cooled and solidified by water to be discharged.
  • the high-temperature gas after the reaction is cooled by the low-temperature gas from the cold gas inlet 8 at the upper portion of the slag gas flow bed 5, and then exits the gasification furnace through the outlet pipe 9 of the slag gas flow bed 5.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Description

复合粉煤气化方法 技术领域
本发明涉及煤化工领域。
背景技术
在煤化工领域， 国内外的.连说续生产的粉煤气化系统， 需要复杂的原料煤处 理、 输送系统， 需要技术复杂、 耐高温、 耐磨损和耐腐蚀的粉煤气化喷嘴， 同 时还需要技术、 材料要求高的气化炉和炉渣处理系统， 使得煤气化系统非常复 杂、 投资巨大、 维护难、 能耗高、 运行成本很高， 己成为制约煤化工发展的重
书
要因素之一。
发明内容
本发明是指在一个粉煤气化系统中同时采用流化床气化技术和熔渣气流床 气化技术。 主要针对在煤化工领域粉煤气化系统需要复杂的原料煤处理、 输送 系统， 需要技术难度大和材料要求高的粉煤气化喷嘴， 需要技术、 材料要求高 的气化炉和炉渣分离系统， 导致煤气化系统非常复杂、 投资巨大、 维护难、 能 耗高、 运行成本高的难题， 发明采用流化床气化炉和熔渣气流床气化炉串联技 术， 普通方式进煤， 粉煤在流化床气化炉内进行初级气化后进入熔渣气流床气 化炉进一步高温熔渣气化， 液态炉渣从气化炉下部自然流入炉渣冷激排出系统， ' 高温反应气被冷激气或冷激水冷激降温后离开气化炉。 使得原料煤进料简单、 无需特殊原料煤处理、 输送系统、 无需特殊的粉煤气化喷嘴， 气、 渣分离简单。 从而降低了煤气化系统的复杂性、 降低了煤气化系统的能耗、 制造和运行成本。
本技术可应用于各种粉煤气化过程。 附图说明
■ 图 1是本发明的原理图。
替换页 （细则第 26条） 具体实施方式
经过初步破碎的粉煤从输煤机 2进入流化床 3， 气化剂氧气， 或氧气和水 蒸气的混合气， 或氧气和二氧化碳的混合气经气化剂入口喷嘴 1送到流化床 3， 在流化床 3 内部进行初步气化后， 含有细颗粒煤粉的粗煤气通过流化床 3的出 口管 4进入熔渣气流床 5， 与通过气化剂喷嘴 7加入的氧气或氧气与水蒸气， 或 氧气与二氧化碳的混合气一起进行高温气化反应， 反应后的熔融炉渣通过熔渣 气流床 5的下部自然流入排渣系统 6， 被水冷却凝固后排出。反应后的高温气体 在熔渣气流床 5的上部被冷激气入口 8来的低温煤气冷却后，通过熔渣气流床 5 的出口管 9离开气化炉。
1
替换页 （细则第 26条)

Claims

权 利 要 求 书
1、 一种复合粉煤气化技术， 其特征是， 在一个粉煤气化系统中同时采 用流化床气化技术和熔渣气流床气化技术。
3
替换页 （细则第 26条)
PCT/CN2011/001193 2010-10-14 2011-07-21 复合粉煤气化方法 WO2012048515A1 (zh)

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CN2010105068089A CN101962576A (zh) 2010-10-14 2010-10-14 复合粉煤气化技术
CN201010506808.9 2010-10-14

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Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101962576A (zh) * 2010-10-14 2011-02-02 邰学林 复合粉煤气化技术
CN102504877A (zh) * 2011-11-07 2012-06-20 邰学林 节能环保型粉煤分级气化工艺
CN102533345B (zh) * 2011-12-14 2014-02-19 中国科学院山西煤炭化学研究所 复合式流化床煤气化的方法及装置
CN102660328A (zh) * 2012-04-25 2012-09-12 邰学林 煤气粉煤节能环保二次气化工艺
CN103194270B (zh) * 2013-03-26 2014-09-03 邰学林 自热式煤气煤粉逆流气流床气化炉
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
CN105838451A (zh) * 2016-04-26 2016-08-10 华陆工程科技有限责任公司 一种串联双床粉煤分步气化方法
CN106118750A (zh) * 2016-08-08 2016-11-16 安徽科达洁能股份有限公司 梯级组合床气化系统
CN107880940B (zh) * 2016-09-30 2023-07-14 中国科学院工程热物理研究所 预热式气化方法及装置

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CN201151710Y (zh) * 2007-10-27 2008-11-19 太原海力丰科技发展有限公司 分级煤气化装置
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CN201574143U (zh) * 2009-11-20 2010-09-08 田原宇 一种粉煤循环流化床分级气化炉
CN101962576A (zh) * 2010-10-14 2011-02-02 邰学林 复合粉煤气化技术

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CN2608507Y (zh) * 2003-02-12 2004-03-31 田原宇 两段粉煤循环流化床气化装置
CN201151710Y (zh) * 2007-10-27 2008-11-19 太原海力丰科技发展有限公司 分级煤气化装置
CN101440310A (zh) * 2007-11-23 2009-05-27 山东科技大学 一种粉煤流化床分级气化的工艺
WO2009116275A1 (ja) * 2008-03-21 2009-09-24 株式会社Ihi ガス化設備の運転方法
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