Method and system for separating hydrogen sulfide in industrial tail gas
A technology of industrial tail gas and separation method, which is applied in the direction of separation method, chemical instrument and method, and separation of dispersed particles, which can solve the problems of high operating cost, environmental pollution by waste, production of by-products or waste, etc., and achieve economic benefits Good, process green and environmental protection effect
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Embodiment 1
[0022] refer to figure 1 , a hydrogen sulfide separation system in industrial tail gas, including a primary cooling unit 10, a secondary cooling unit 20, a gas-liquid separator 30, a liquid storage unit 40 and an absorption unit 50.
[0023] The primary cooling unit 10 is used for preliminary cooling of industrial tail gas, including a first tail gas inlet 11 and a first tail gas outlet 12 , a first cold source inlet 13 and a first cold source outlet 14 . Specifically, the primary cooling unit 10 can be a tube-and-tube heat exchanger, so that the first exhaust gas inlet 11 and the first exhaust gas outlet 12 can communicate with the tube side of the tube-and-tube heat exchanger, and the first cold source inlet 13 and The outlet 14 of the first cold source can communicate with and communicate with the shell side of the shell-and-tube heat exchanger, so that the first cold source and industrial exhaust gas can exchange heat in the shell-and-tube heat exchanger.
[0024] The sec...
Embodiment 2
[0031] A method for separating hydrogen sulfide in industrial tail gas, comprising the steps of:
[0032] (1) Using the circulating water as the cooling source, the industrial tail gas is cooled by the primary cooling unit 10 to obtain the primary cooling tail gas with a temperature of 0° C. to 10° C., and enter the secondary cooling unit 20;
[0033] (2) Using liquid nitrogen as a cooling source, the secondary cooling unit 20 is used to perform secondary cooling on the primary cooling tail gas to obtain cryogenic tail gas at a temperature of -80°C to -75°C, and enter the gas-liquid separator 30;
[0034] (3) Use the gas-liquid separator 30 to perform gas-liquid separation on the cryogenic tail gas, wherein the liquid leads to the liquid storage unit 40, and the gas passes to the secondary cooling unit 20 to be heated to 5-10°C by heat exchange, and then absorbed Unit 50 is discharged after treatment.
[0035] After testing, the hydrogen sulfide content in the liquid storage ...
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