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Comprehensive utilization process for low-carbon-emission Fischer-Tropsch synthesis tail gas

一种费托合成、碳排放的技术,应用在氢/合成气生产、碳氢化合物、碳氢化合物等方向,能够解决尿素合成装置建设成本高昂、尾气没有给予关注、设备投资高等问题,达到提高能源利用效率、解决氢源不足、降低能源成本的效果

Active Publication Date: 2012-10-17
WUHAN KAIDI ENG TECH RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Chinese patents CN1354779A and CN1761734A respectively announced a process for Fischer-Tropsch synthesis to produce liquid hydrocarbons, but did not pay attention to the tail gas produced in the process
[0005] In the method disclosed in Chinese patent CN101538483A, the CO produced in the process is 2 Supply the urea synthesis section, so as to realize the CO 2 Nearly zero emissions, but a special synthetic ammonia section is required for this purpose, and the construction cost of the urea synthesis plant is high
However, the processes of gasification, shifting and decarbonization are complicated and the investment in equipment is relatively high.

Method used

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  • Comprehensive utilization process for low-carbon-emission Fischer-Tropsch synthesis tail gas
  • Comprehensive utilization process for low-carbon-emission Fischer-Tropsch synthesis tail gas
  • Comprehensive utilization process for low-carbon-emission Fischer-Tropsch synthesis tail gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0050] Embodiment one has used the raw material gas identical with comparative example, and according to figure 1 The process shown returns the produced hydrogen before the shift reactor.

[0051] 1) Raw gas refers to the gas containing carbon monoxide and hydrogen produced by gasification of coal or biomass, and the 5890NM 3 Raw material gas with a low hydrogen-to-carbon ratio per hour, wherein the molar ratio of hydrogen to carbon monoxide in the raw gas is 0.1, and it is transported to the shift reactor. Under the action of a catalyst, it is converted into hydrogen and carbon dioxide, and the 2120NM 3 / h of carbon monoxide is converted into carbon dioxide and the same volume of hydrogen is generated. After removing carbon dioxide, a shift gas of 4480 NM is produced for Fischer-Tropsch synthesis. 3 / h, wherein the molar ratio of hydrogen to carbon monoxide in the shift gas is 1.7, and the effective synthesis gas accounts for more than 88% of the total gas volume.

[0052]...

Embodiment 2

[0062] Adopt the tail gas treatment mode identical with embodiment one, still according to figure 1 The process shown returns the produced hydrogen before the shift reactor.

[0063] 1) Raw gas refers to the gas containing carbon monoxide and hydrogen produced by gasification of coal or biomass, and the 5950NM 3 Raw material gas with a low hydrogen-to-carbon ratio per hour, wherein the molar ratio of hydrogen to carbon monoxide in the raw gas is 1.1, and it is transported to the shift reactor. Under the action of a catalyst, it is converted into hydrogen and carbon dioxide, and the 256NM 3 / h of carbon monoxide is converted into carbon dioxide and the same volume of hydrogen is generated. After removing carbon dioxide, a shift gas of 4530NM is produced for Fischer-Tropsch synthesis. 3 / h, where the molar ratio of hydrogen to carbon monoxide in the shift gas is 1.43, and the effective synthesis gas accounts for more than 88% of the total gas volume.

[0064] 2) After mixing ...

Embodiment 3

[0074] Embodiment three has used the change of gas composition and gas volume as shown in table 4 raw material gas, and according to figure 2 The process shown returns the produced hydrogen after the shift reactor.

[0075] 1) Raw gas refers to the gas containing carbon monoxide and hydrogen produced by gasification of coal or biomass, and the 5900NM 3 Raw material gas with a low hydrogen-to-carbon ratio per hour, wherein the molar ratio of hydrogen to carbon monoxide in the raw gas is 2.2, which is transported to the shift reactor. Under the action of a catalyst, it is converted into hydrogen and carbon dioxide, and the 300NM 3 / h of carbon monoxide is converted into carbon dioxide and the same volume of hydrogen is generated. After removing carbon dioxide, a shift gas of 5090NM is produced for Fischer-Tropsch synthesis. 3 / h, wherein the molar ratio of hydrogen to carbon monoxide in the shift gas is 3.0, and the effective synthesis gas accounts for more than 95% of the to...

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Abstract

The invention discloses a comprehensive utilization process for a low-carbon-emission Fischer-Tropsch synthesis tail gas. The process is used for converting the non-circular tail gas generated after the Fischer-Tropsch synthesis reaction into synthesis gas containing hydrogen through water vapor reforming, and then separating and extracting high-purity hydrogen from the synthesis gas containing hydrogen for use. The comprehensive utilization process comprises the following steps: 1) obtaining converted gas through a water vapor conversion reaction, 2) obtaining a hydrocarbon fuel through a Fischer-Tropsch synthesis reaction, 3) converting a hydrocarbon compound containing two or more than two carbon atoms into methane after a pre-reforming reaction, 4), converting methane and water vapor into hydrogen and carbon monoxide through a reforming reaction, 5) separating gases respectively containing hydrogen and carbon monoxide, 6) and providing heat for a reforming reactor. The process disclosed by the invention can be used for effectively utilizing the Fischer-Tropsch synthesis tail gas, especially the tail gas containing a large amount of inert components, and converting the tail gas into the hydrogen for use. Meanwhile, the comprehensive utilization process disclosed by the invention can be used for effectively utilizing residual combustible components after the hydrogen in the reforming gas is separated, thereby enhancing the utilization efficiency of the energy.

Description

technical field [0001] The invention relates to a Fischer-Tropsch tail gas treatment process containing inert gas components, in particular to a low-carbon discharge Fischer-Tropsch synthesis tail gas comprehensive utilization process. Background technique [0002] Fischer-Tropsch synthesis is the process of producing fuel and chemicals from synthesis gas formed by converting fossil energy such as coal and natural gas or renewable energy such as biomass under the action of a catalyst. It plays an important role in reducing dependence on petroleum route energy and chemical production and utilizing clean energy. In particular, the Fischer-Tropsch synthesis process, which uses biomass as raw material to produce syngas, has greatly reduced the dependence on fossil energy. [0003] In addition to long-chain liquid hydrocarbons, Fischer-Tropsch products also include low-carbon hydrocarbons with three carbon atoms (C3) and below, and become the main component of tail gas, of which...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/38
CPCC10K1/005C01B3/34C01B2203/142C10K3/04C01B2203/0805C10G2/30C10K3/06C01B3/38C01B2203/047C01B2203/0233C01B3/16C01B2203/0283C01B2203/04C01B2203/0445C01B2203/0475C01B2203/062C01B2203/0827C01B2203/1241C10G2/332C01B2203/84C07C1/0485C07C4/06C07C2523/755C10G2/00Y02P20/10
Inventor 陈义龙蒯平宇龚焱詹晓东张岩丰金家琪
Owner WUHAN KAIDI ENG TECH RES INST CO LTD
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