Radian Corporation

Gas Research Institute

Timothy W Trofe

Frank J Castaldi

Kevin M Adams

Gordon C Page

David W DeBerry

A method and apparatus for the removal of hydrogen sulfide (H.sub.2 S) from gaseous streams, particularly concentrations of H.sub.2 S lower than 100 ppm. The invention is particularly useful for removing H.sub.2 S from natural gas. The invention involves contacting a gaseous stream containing hydrogen sulfide with a sorbent solution comprising a substantially non-aqueous solvent having a low vapor pressure and a high donor number, such as dimethyl sulfoxide, a concentration of a polyvalent reducible metal ion in an oxidative state sufficient to oxidize the hydrogen sulfide to form at least one soluble sulfur compound, such as Fe.sup.3+, and a counter-ion for the metal ion, such as Cl.sup.- ; and regenerating the oxidative state of the metal ion reduced by the hydrogen sulfide.

Composition and process for the removal of hydrogen sulfide from gaseous

Free cyanide-containing wastewater is treated to destroy the free cyanide content thereof by the step of treating said water with sulfur in the form of polysulfide in an integrated process wherein thiocyanate is also eliminated to produce a non-hazardous wastewater effluent and treating the wastewater in a second step with cultures of bacteria of the genus Thiobacillus in combination with nitrifying bacteria which oxidize ammonia to nitrite to nitrate. The first step is preferably carried out in the presence of a cationic surfactant, preferably a quaternary cationic surfactant, as a catalyst.

Process for wastewater treatment

Free cyanide-containing wastewater is treated to destroy the free cyanide content thereof by the step of treating said water with sulfur in the form of polysulfide in an integrated process wherein thiocyanate is also eliminated to produce a non-hazardous wastewater effluent and treating the wastewater in a second step with cultures of bacteria of the genus Thiobacillus in combination with nitrifying bacteria which oxidize ammonia to nitrite and nitrite to nitrate. The first step is preferably carried out in the presence of added metallic zinc.

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Austin, TX, United States of America

Timothy W Trofe