Process for the removal of H2 S and CO2 from gaseous streams

Claim 2

A process for the removal of H 2 S and CO 2 from a sour gaseous stream comprising: A. contacting the sour gaseous stream with a lean CO 2 -selective absorbent mixture containing an effective amount of the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, and producing a sweet gaseous stream and an absorbent admixture containing absorbed CO 2 , sulfur, and the Fe (II) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, B. removing sulfur from the absorbent admixture, and leaving a solution containing absorbed CO 2 and the Fe (II) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, C. stripping the solution containing absorbed CO 2 and the said Fe (II) chelate and regenerating the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid in said solution with an oxygen-containing gas, producing a lean CO 2 -selective absorbent solution containing the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, and D. returning the lean CO 2 -selective absorbent solution containing the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid to step A.

Claim 3

The method of claim 1 wherein the absorbent is selected from the group consisting of propylene carbonate, tetra-ethylene glycoldimethyl ether, N-methyl pyrrolidone, sulfolane, methyl isobutyl ketone, 2,4-pentanedione, 2,5-hexanedione, diacetone alcohol, hexyl acetate, cyclohexanone, mesityl oxide, and 4-methyl-4-methoxy-pentone-2.

Claim 4

The method of claim 1 wherein the stream from which the H 2 S and CO 2 are removed is selected from naturally occurring gases, synthesis gases, process gases, and fuel gases.

Claim 5

The method of claim 3 wherein the sour gaseous stream is a stream derived from the gasification and partial oxidation of a liquid hydrocarbon.

Claim 6

The process of claim 3 wherein heat is supplied in step (C) to assist in regeneration.

Claim 7

The method of claim 3 wherein the stream from which the H 2 S and CO 2 are removed is a fuel gas stream produced by gasification of a material selected from coal, petroleum, oil shale, or tar sands.

Claim 8

The method of claim 6 wherein the sour gaseous stream is a stream derived from the gasification of coal.

Claim 9

A process for the removal of H 2 S and CO 2 from a sour gaseous stream comprising: A. contacting the sour gaseous stream with a lean CO 2 -selective absorbent solution containing an effective amount of the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, and producing a sweet gaseous stream and an absorbent mixture containing absorbed CO 2 , sulfur, and the Fe (II) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, B. stripping the solution containing absorbed CO 2 , sulfur, and the said Fe (II) chelate and regenerating the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid in said solution with an oxygen-containing gas, producing a lean CO 2 -selective absorbent solution containing the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, and sulfur, C. removing sulfur from the lean CO 2 -selective absorbent solution containing the sulfur and the Fe III chelate of N-(2-hydroxyethyl) ethylene diamine triactic acid, and leaving a lean CO 2 -selective absorbent solution containing the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, and D. returning the lean CO 2 -selective absorbent solution containing the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid to step A.

Claim 10

A process for the removal of H 2 S and CO 2 from a sour gaseous stream comprising: A. contacting the sour gaseous stream with a lean CO 2 -selective absorbent solution containing an effective amount of the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, and producing a sweet gaseous stream and an absorbent mixture containing absorbed CO 2 , sulfur, and the Fe (II) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, B. stripping the solution containing absorbed CO 2 , sulfur, and the said Fe (II) chelate and regenerating the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid in said solution with an oxygen-containing gas, producing a lean CO 2 -selective absorbent solution containing the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, and sulfur, C. removing sulfur from the lean CO 2 -selective absorbent solution containing the sulfur and the Fe III chelate of N-(2-hydroxyethyl) ethylene diamine triactic acid, and leaving a lean CO 2 -selective absorbent solution containing the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid, and D. returning the lean CO 2 -selective absorbent solution containing the Fe (III) chelate of N-(2-hydroxyethyl) ethylene diamine triacetic acid to step A.

Claim 11

The method of claim 8 wherein the absorbent is selected from the group consisting of propylene carbonate, tetra-ethylene glycoldimethyl ether, N-methyl pyrrolidone, sulfolane, methyl isobutyl ketone, 2,4-pentanedione, 2,5-hexanedione, diacetone alcohol, hexyl acetate, cyclohexanone, mesityl oxide, and 4-methyl-4-methoxy-pentone-2.

Claim 12

The method of claim 8 wherein the stream from which the H 2 S and CO 2 are removed is selected from naturally occurring gases, synthesis gases, process gases, and fuel gases.

Claim 13

The process of claim 10 wherein heat is supplied in step (B) to assist in regeneration.

Claim 14

The method of claim 10 wherein the sour gaseous stream is a stream derived from the gasification and partial oxidation of a liquid hydrocarbon.

Claim 15

The method of claim 10 wherein the stream from which the H 2 S and CO 2 are removed is a fuel gas stream produced by gasification of a material selected from coal, petroleum, oil shale, or tar sands.

Claim 16

The method of claim 13 wherein the sour gaseous stream is a stream derived from the gasification coal.