Activated carbon process for removing hydrogen sulfide from gase

Chemistry of inorganic compounds – Modifying or removing component of normally gaseous mixture – Carbon dioxide or hydrogen sulfide component

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423230, 423233, 42324403, 42324406, 423576, 4235762, 4235768, C01B 1716

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active

052563847

ABSTRACT:
To a gas which contains H.sub.2 S and water vapor and which is to be desulfurized oxygen is added at such a rate that the gas contains 1 to 20 moles O.sub.2 per mole of H.sub.2 S. At a temperature in the range of 50.degree. to 180.degree. C. the gas is contacted with activated carbon, which is thus laden with elemental sulfur and with at least 3% by weight sulfuric acid. In a suitable processing, the gas which is to be desulfurized and contains at least 1000 ppm H.sub.2 S+SO.sub.2 is initially passed at a temperature from 100.degree. to 180.degree. C. through a catalytic prepurifier, in which elemental sulfur is adsorbed on a high-metal-oxide catalyst, oxygen is admixed to the gas coming from the prepurifier and the gas at a temperature of 50.degree. to 180.degree. is contacted with the activated carbon for a final desulfurization.

REFERENCES:
patent: 4141962 (1979-02-01), Dupuy et al.
patent: 4219537 (1980-08-01), Steiner
patent: 4263271 (1981-04-01), Henning et al.
patent: 5039507 (1991-08-01), Sturm
"Claus Sulfur Plant Operation for the Maintenance of Catalyst Activity" by William S. Norman presented to Gas Conditioning Conference on Mar. 8, 1976 in Norman, Oklahoma U.S.A.; Kaiser Aluminum & Chemical Corp. Baton Rouge, Louisana U.S.A.

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