The utility model relates to the technical field of
chemical engineering, and discloses a low-pressure separated gas
recovery system of a
coal tar hydrogenation device for
chemical engineering. The
system comprises a liquid-phase hydrogenation cold low-pressure separation tank, a hydrofining cold low-pressure separation tank, a hydrofining cold high-pressure separation tank, a low-pressure separation gas desulfurization
tower and the like. The upper part of the desulfurization
tower is connected with a desulfurization barren liquor
solvent pump, and the bottom of the desulfurization
tower is connected with a desulfurization pregnant solution
desorption regeneration
system and is connected with the desulfurization barren liquor
solvent pump and the desulfurization pregnant solution
desorption regeneration system. The top of the desulfurization tower is connected with a low-pressure gas vapor-liquid separator, and is subsequently connected with a series of equipment such as a low-pressure gas
hydrogen extraction adsorption tower. According to the system, sulfides in low-pressure gas are removed by using a desulfurization barren solution, and a desulfurization pregnant solution is subjected to
desorption regeneration and then is recycled. The desulfurized low-pressure separated gas is subjected to the steps of gas-liquid separation,
hydrogen extraction adsorption and the like, and the purity of gas
hydrogen at the outlet of the top of the hydrogen extraction adsorption tower can be controlled to be greater than 95%, so that the effective utilization of energy is realized, the
coal tar hydrogenation and hydrogen cost is reduced, the energy waste, environmental
pollution and potential safety hazards are reduced, the
ecological environment is improved, and the production safety is improved.