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A kind of preparation method of synthesis gas

A synthesis gas and gas cabinet technology, applied in chemical instruments and methods, hydrogen production, gas fuel, etc., can solve problems such as insufficient utilization, unbalanced component ratio, complicated operation and operation, and achieve easy operation and management, hydrogen Controllable carbon ratio and single process

Active Publication Date: 2017-09-19
SEDIN ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, in addition to the production of synthetic ammonia and methanol, coke oven gas has a surplus of nearly 30 billion cubic meters of coke oven gas per year. Due to the characteristics of "more hydrogen and less carbon" in the composition of coke oven gas, the energy utilization rate of coke oven gas at this stage is about 55%. , resulting in huge waste of energy and environmental pollution
[0005] From the characteristics of coke oven gas and coal-to-gas, it can be seen that the production of synthetic ammonia, natural gas, methanol, ethylene glycol, low-carbon olefins, synthetic oil and other products from coke oven gas or coal-to-gas alone has unbalanced component ratios and utilization Insufficient problem: Coke oven gas has more hydrogen and less carbon, and if it is used alone for synthetic products, there will inevitably be a large amount of hydrogen surplus, or additional carbon sources need to be added; while coal-based gas has more carbon and less hydrogen, and if it is used alone, there will be a large amount of carbon surplus, or Requires an additional large amount of supplemental hydrogen source
[0006] At present, in actual production, for the characteristics of coal-based gas with more carbon and less hydrogen, a reasonable hydrogen-carbon ratio is generally obtained through water vapor shift; coke oven gas has more hydrogen and less carbon, and high methane content, and methane carbon dioxide reforming is usually used However, whether it is water-steam shift or methane reforming, there are problems such as high investment, high energy consumption, and complicated operation.

Method used

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  • A kind of preparation method of synthesis gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] The coke oven gas produced by the top-loading coke oven (volume percentage composition is H 2 : 57%, CH 4 : 28%, CO+CO 2 :11%,N 2 : 4%) and 40% volume of coal-to-gas produced by pressurized gasification of crushed coal (volume percentage composition is CO: 51%, H 2 : 24%, CO 2 : 13%, CH4 : 12%, H 2 S: 0.2%) into the gas holder, the molar flow ratio of coke oven gas and coal-based gas is 2.5:1, and another part of 60% of the volume of coal-based gas enters methane reforming, at a temperature of 630 ° C, a pressure of 1.5 MPa, using nickel Reforming under the condition of base catalyst to form a crude raw material gas with a hydrogen-to-carbon molar ratio of 2.32. The crude raw gas is compressed and washed with methanol at a low temperature to remove H under the conditions of pressure 4.0MPa and temperature -47°C. 2 S and CO 2 and other impurities to obtain H 2 S content is less than 0.1ppm, CO 2 Feed gas with a content of less than 20ppm, the removed H 2 S desul...

Embodiment 2

[0038] The coke oven gas (volume percentage composition as H 2 : 61%, CH 4 : 22%, CO+CO 2 :12%,N 2 : 5%) and about 30% volume of coal-to-gas produced by Lurgi gasifier (volume percentage composition is CO: 54%, H 2 : 21%, CO 2 : 14%, CH 4 : 11%, H 2 S: 0.25%) into the gas holder, the molar flow ratio of coke oven gas and coal gas is 5.0:1, and another part of 70% of the volume of coal gas enters methane reforming, at a temperature of 650 ° C, a pressure of 2.1 MPa, using nickel reforming under the condition of base catalyst to form a crude raw material gas with a hydrogen-to-carbon molar ratio of 3.41. After being compressed, the crude raw material gas enters low-temperature methanol washing and purification, and removes H at a pressure of 4.3 MPa and a temperature of -45°C. 2 S and CO 2 and other impurities to obtain H 2 S content is less than 0.1ppm, CO 2 Feed gas with a content of less than 20ppm, the removed H 2 S desulfurization recovery, CO removal 2 The gas i...

Embodiment 3

[0040] The coke oven gas (volume percentage composition as H 2 : 49%, CH 4 : 27%, CO+CO 2 :17%, N 2 : 7%) and about 80% volume of coal-to-gas produced by Texaco coal-water slurry gasifier (volume percentage composition is CO: 60%, H 2 : 22%, CO 2 : 9%, CH 4 : 9%, H 2 S: 0.3%) into the gas holder, the molar flow ratio of coke oven gas and coal gas is 4.0:1, and another part of about 20% of the volume of coal gas enters methane reforming, at a temperature of 680°C and a pressure of 1.8MPa, using Reforming is carried out under the condition of nickel-based catalyst to form a crude raw material gas with a hydrogen-to-carbon ratio of 2.14. The crude raw material gas is purified by thermal alkali method after compression, and H is removed at a pressure of 1.5 MPa and a temperature of 99 °C. 2 S and CO 2 and other impurities to obtain H 2 S content is less than 0.1ppm, CO 2 Feed gas with a content of less than 20ppm, the removed H 2 S desulfurization recovery, CO removal 2...

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Abstract

A synthesis gas preparation method is to pass coke oven gas and part of the coal-based gas into the gas cabinet for mixing, and the other part of the coal-based gas to undergo methane reforming for reforming, and then combine the reformed gas with the mixed gas passed through the gas cabinet and compress it. Purify, remove impurities such as H2S and remaining CO2, remove hydrogen sulfide, desulfurize and recover, and remove CO2 gas to vent. The purified raw material gas is subjected to methane separation, and the methane gas is separated to produce liquefied natural gas products or compressed natural gas products, and the methane gas is separated to obtain pure synthesis gas that meets the requirements of the hydrogen-carbon ratio of the downstream products of the synthesis. The invention has the advantage of realizing comprehensive utilization of coal gas and coke oven gas.

Description

technical field [0001] The invention belongs to a method for preparing synthesis gas. technical background [0002] Synthesis gas is a kind of raw material gas with carbon monoxide and hydrogen as the main components, which is used as a chemical raw material. Syngas is widely used and is the most basic raw material for synthetic ammonia, natural gas, methanol, ethylene glycol, light olefins, synthetic oil and other products. Syngas has a wide range of raw materials. It is produced by the gasification of carbonaceous minerals such as solid fuels such as coal and charcoal. It can also be produced from light hydrocarbons such as natural gas and naphtha. It can also be produced from heavy oil through partial oxidation. [0003] The composition (volume %) of synthesis gas produced by various methods is very different: H2: 32-67, CO: 10-57, CO2: 2-28, CH4: 0.1-14, N2: 0.6-23. In addition, there are trace amounts of harmful components such as H2S, COS, and HCN. The synthesis gas...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/02C01B3/38C10L3/08
Inventor 李晓崔晓曦曹会博马英民
Owner SEDIN ENG
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