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
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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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