Process for production of dimethyl ether and combined production of natural gas and urea from coal-based synthetic gas and coke oven gas
A technology for coal-based synthesis gas and coke oven gas, which is applied in the dehydration of hydroxyl-containing compounds to prepare ethers, the preparation of organic compounds, and the preparation of ethers, etc., can solve problems such as hydrogen supplementation, achieve strong absorption capacity, improve utilization rate, and increase circulation capacity. small effect
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Embodiment 1
[0034] The coke oven gas produced by the tamping coke oven (volume percentage is composed of H 2 : 53%, CH 4 : 26%, CO+CO 2 :15%, N 2 : 6%) and coal-based syngas produced by Lurgi furnace (volume percentage composition is CO: 52%, H 2 : 23%, CO 2 : 14%, CH 4 : 11%, H 2 S: 0.2%) is passed into the gas cabinet at a volume ratio of 0.7:1 and fully mixed to form a hydrogen-carbon molar ratio H 2 / C=0.99 meets the crude raw material gas of dimethyl ether synthesis;
[0035] Crude raw material gas is compressed and washed with methanol at low temperature to remove H at -42°C and 4.0MPa 2 S and other impurities, get H 2 The raw material gas with S content less than 0.1ppm, the hydrogen sulfide desulfurization and recovery after removal, the purified crude raw material gas adopts the cryogenic separation technology of American Chemtex and Berkeley Weiqi Company, and enters the cryogenic separation, at a temperature of -156°C , the pressure is 4.0MPa to separate methane to mak...
Embodiment 2
[0037] The coke oven gas produced by the tamping coke oven (volume percentage is composed of H 2 : 61%, CH 4 : 23%, CO+CO 2 :11%,N 2 : 5%) and coal-based synthesis gas produced by pressurized gasification of crushed coal (volume percentage composition is CO: 59%, H 2 : 20%, CO 2 : 12%, CH 4 : 9%, H 2 S: 0.23%) is passed into the gas cabinet at a volume ratio of 1:1 and fully mixed to form a hydrogen-carbon molar ratio H 2 / C=1.24 meets the crude raw material gas of dimethyl ether synthesis;
[0038] Crude raw gas is compressed and washed with methanol at low temperature to remove H at -46°C and 4.5MPa 2 S and other impurities, get H 2 The raw material gas with S content less than 0.1ppm, the hydrogen sulfide desulfurization and recovery after removal, the purified raw material gas adopts the cryogenic separation technology of American Chemtex and Berkeley Weiqi Company, and enters the methane cryogenic separation, at a temperature of -152 ℃, pressure 4.5MPa to separat...
Embodiment 3
[0040] The coke oven gas produced by the top-loading coke oven (volume percentage composition is H 2 : 52%, CH 4 : 27%, CO+CO 2 :16%,N 2 : 5%) and the coal-based synthesis gas produced by Texaco coal-water slurry gasifier gasification (volume percentage composition is CO: 58%, H 2 : 20%, CO 2 : 9%, CH 4 : 13%, H 2 S: 0.21%) is passed into the gas cabinet at a volume ratio of 1.8:1 and fully mixed to form a hydrogen-carbon molar ratio H 2 / C=1.39 meets the crude raw material gas of dimethyl ether synthesis;
[0041] The crude raw material gas is compressed and then enters into the NHD method for purification. Under the conditions of pressure 2.5MPa and temperature 2°C, impurities such as H2S are removed to obtain H 2 For raw material gas with S content less than 0.1ppm, the hydrogen sulfide removed is desulfurized and recovered, and the purified crude raw gas enters supercritical methane separation, and the methane is separated in a supercritical state with a pressure of...
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