Method of removing hydrogen sulfide from gases utilizing a polyvalent metal chelate of nitrilotriacetic acid and electrolytically regenerating the solution

Claim 2

A process for the removal of H 2 S from a sour gaseous stream comprising (a) contacting the sour gaseous stream in a contacting zone with an aqueous reaction solution at a temperature below the melting point of sulfur, the solution containing an effective amount of an oxidizing polyvalent metal chelate of nitrilotriacetic acid, and mixtures thereof, and producing a sweet gas stream and an aqueous admixture containing crystalline sulfur, hydrogen ions, and reduced polyvalent metal chelate or chelates of nitrilotriacetic acid; said contacting zone comprising an anode section of an electrochemical cell, said cell also comprising a separate chathode section containing a cathode connected through an external electrical connection to the anode, the anode section and the cathode section being separated by a hydrogen ion permeable barrier; (b) oxidizing the reduced polyvalent metal chelate or chelates of nitrilotriacetic acid in the aqueous reaction solution at the anode by supplying direct current to said cell, concomitantly allowing hydrogen ions to migrate to the cathode and producing hydrogen at the cathode; (c) removing sulfur from the aqueous reaction solution, and hydrogen from the cathode section.

Claim 3

A process for the removal of H 2 S from a sour gaseous stream comprising (a) contacting the sour gaseous stream in a contacting zone with an aqueous reaction solution at a temperature below the melting point of sulfur, the solution containing an effective amount of an oxidizing polyvalent metal chelate of nitrilotriacetic acid, and mixtures thereof, and producing a sweet gas stream and an aqueous admixture containing crystalline sulfur, hydrogen ions, and reduced polyvalent metal chelate or chelates of nitrilotriacetic acid; (b) removing sulfur from the aqueous admixture; (c) regenerating aqueous admixture from step (b) electrolytically by passing admixture from step (b) through the anode section of an electrochemical cell and supplying direct current to said cell to oxidize reduced polyvalent metal chelate or chelates in the admixture at the anode, and producing a regenerated aqueous admixture containing regenerated oxidizing polyvalent metal chelate or chelates of nitrilotriacetic acid, the anode section and the cathode section of said cell being separated by a hydrogen ion permeable barrier, concomitantly allowing hydrogen ions to migrate to the cathode section, and producing hydrogen at the cathode; (d) removing regenerated aqueous admixture from said anode section, and molecular hydrogen from said cathode section; and (e) returning regenerated aqueous admixture to the contacting zone.

Claim 4

A process for the removal of H 2 S from a sour gaseous stream comprising (a) contacting the sour gaseous stream in a contacting zone with an aqueous reaction solution at a temperature below the melting point of sulfur, the solution containing an effective amount of an oxidizing polyvalent metal chelate of nitrilotriacetic acid, and mixtures thereof, and producing a sweet gas stream and an aqueous admixture containing crystalline sulfur, hydrogen ions, and reduced polyvalent metal chelate or chelates of nitrilotriacetic acid; (b) removing sulfur from the aqueous admixture; (c) regenerating aqueous admixture from step (b) electrolytically by passing admixture from step (b) through the anode section of an electrochemical cell and supplying direct current to said cell to oxidize reduced polyvalent metal chelate or chelates in the admixture at the anode, and producing a regenerated aqueous admixture containing regenerated oxidizing polyvalent metal chelate or chelates of nitrilotriacetic acid, the anode section and the cathode section of said cell being separated by a hydrogen ion permeable barrier, concomitantly allowing hydrogen ions to migrate to the cathode section, and producing hydrogen at the cathode; (d) removing regenerated aqueous admixture from said anode section, and molecular hydrogen from said cathode section; and (e) returning regenerated aqueous admixture to the contacting zone.

Claim 5

The process of claim 2 wherein the oxidizing polyvalent metal chelate of nitrilotriacetic acid is the ferric chelate of nitrilotriacetic acid.

Claim 6

The process of claim 1 wherein the aqueous reaction solution comprises a liquid absorbent selective for CO 2 .

Claim 7

The process of claim 2 wherein the aqueous reaction solution comprises a liquid absorbent selective for CO 2 .

Claim 8

The process of claim 3 wherein the aqueous reaction solution comprises a liquid absorbent selective for CO 2 .