Abstract Hydrogen sulfide is removed from a mixture of gases including carbon dioxide by passing the mixture over an immobilized liquid membrane in intimate contact with a hydrophobic, microporous gas, permeable barrier and absorbing in a liquid solution hydrogen sulfide passing through the membrane. In a sweep of hot carbonate solution, a nearly stagnant boundary layer adjacent the gas permeable barrier absorbs acid gases by reaction and diffusion, maintaining low hydrogen sulfide partial pressure at the outlet side of the barrier. Alternatively, the sweep may comprise an aqueous solution containing a redox agent which converts absorbed hydrogen sulfide into sulfur, or an ethanol amine solution. The apparatus exhibits low permeability to carbon dioxide and high permeability to hydrogen sulfide.
A method of selectively removing hydrogen sulfide from a mixture of gases including carbon dioxide, comprising: contacting an immobilized liquid membrane with said mixture to allow facilitated transport of hydrogen sulfide through said membrane to a porous gas-permeable barrier; passing gases emerging from said membrane through said gas-permeable barrier; absorbing in a sweep liquid the gases emerging from said gas-permeable barrier; and said sweep liquid comprising a liquid selected from a group consisting of a hot carbonate solution, a solution of redox agent which converts hydrogen sulfide to sulfur, and an ethanol amine solution.
Claim 2
Independent Claim
94 words
A method of selectively removing hydrogen sulfide from a mixture of gases including carbon dioxide, comprising: contacting an immobilized liquid membrane with said mixture to allow facilitated transport of hydrogen sulfide through said membrane to a porous gas-permeable barrier; passing gases emerging from said membrane through said gas-permeable barrier; absorbing in a sweep liquid the gases emerging from said gas-permeable barrier; and said sweep liquid comprising a liquid selected from a group consisting of a hot carbonate solution, a solution of redox agent which converts hydrogen sulfide to sulfur, and an ethanol amine solution.
Claim 3
Dependent Claim
41 words
The method of claim 1 including the step of regenerating said sweep liquid by contacting an additional porous gas permeable barrier with said sweep liquid and absorbing in a steam sweep the gases emerging from said additional porous gas permeable barrier.
Claim 4
Dependent Claim
21 words
The method of claim 1, wherein the sweep liquid is supplied at approximately the same pressure as the mixture of gases.