Process for producing liquefied natural gas by using coke-oven gas
A technology for liquefied natural gas and coke oven gas, which is applied in the petroleum industry, gas fuel, fuel, etc., can solve the problems of large volume of natural gas, low methane yield, and high logistics cost, and achieves improved economic benefits, reduced production costs, and reduced environmental The effect of pollution
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Embodiment 1
[0025] The coke oven gas from the coking plant at 30KpaG, the methane-rich gas separated by cryogenic liquefaction and the evaporated gas from the liquefied natural gas storage tank are evenly mixed; they are sent to the water-sprayed screw compressor for two-stage compression, so that the pressure of the mixed raw material gas is changed from 30KpaG Boost the pressure to 0.9MpaG; then remove impurity tar, benzene, naphthalene, ammonia and hydrogen cyanide through temperature swing adsorption; the purge gas used in temperature swing adsorption comes from the pretreated mixed raw material gas, and the amount used is 1% of the volume of the mixed raw material gas / 10, the purge gas is treated by electric coke capture and benzene-naphthalene washing, and then returned to the coking plant as fuel gas.
[0026] The mixed raw material gas is then adsorbed by iron oxide to remove hydrogen sulfide in the mixed raw material gas, the mixed raw material gas is hydrogenated by iron molybde...
Embodiment 2
[0030] The coke oven gas from the coking plant under 30KpaG, the methane-rich gas separated by cryogenic liquefaction, the boil-off gas from the liquefied natural gas storage tank, and about 2692Nm from the chemical plant 3 / h with CO 2 85% (V / V%) exhaust gas, uniformly mixed; sent to the water-jet screw compressor for two-stage compression, so that the pressure of the mixed raw material gas is increased from 30KpaG to 0.9MpaG; and then the impurities tar, benzene, Naphthalene, ammonia and hydrogen cyanide; the purge gas used for temperature swing adsorption comes from the pretreated mixed raw material gas, and the amount used is 1 / 10 of the volume of the mixed raw material gas. Back to the coking plant to make fuel gas.
[0031] The mixed raw material gas is then adsorbed by iron oxide to remove hydrogen sulfide in the mixed raw material gas, the mixed raw material gas is hydrogenated by iron molybdenum and nickel molybdenum, and the organic sulfur in the mixed raw material...
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