Method of removing hydrogen sulfide from gases utilizing a polyvalent metal chelate solution 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 reactant comprising an oxidizing polyvalent metal chelate of an acid having the formula ##STR3## wherein from two to four of the groups Y are selected from acetic and propionic acid groups; from zero to two of the groups Y are selected from 2-hydroxy ethyl, 2-hydroxy propyl, and ##STR4## wherein X is selected from acetic acid and propionic acid groups; and R is ethylene, propylene or isopropylene or alternatively cyclohexane or benzene where the two hydrogen atoms replaced by nitrogen atoms are in the 1,2 position, and mixtures thereof; and producing a sweet gas stream and an aqueous reaction solution containing crystalline sulfur, hydrogen ions, and reduced polyvalent metal chelate or chelates of said acid; said contacting zone comprising an anode section of an electrochemical cell, said cell also comprising a separate cathode 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 said acid in the aqueous reaction solution at the anode by supplying direct current to said cell and allowing hydrogen ions to migrate to the cathode, concomitantly supplying oxygen to the cathode and forming water at the cathode; (c) removing sulfur from the aqueous reaction solution, and water 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 reactant comprising an oxidizing polyvalent metal chelate of an acid having the formula ##STR5## wherein from two to four of the groups Y are selected from acetic and propionic acid groups; from zero to two of the groups Y are selected from 2-hydroxy ethyl, 2-hydroxy propyl, and ##STR6## wherein X is selected from acetic acid and propionic acid groups; and R is ethylene, propylene or isopropylene or alternatively cyclohexane or benzene where the two hydrogen atoms replaced by nitrogen atoms are in the 1,2 position, 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 said acid; (b) removing sulfur from the 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 the reduced chelate or chelates in the admixture at the anode and producing a regenerated aqueous admixture containing regenerated oxidizing reactant, the anode section and the cathode section of the electrochemical cell being separated by a hydrogen ion permeable barrier; concomitantly supplying oxygen to the cathode section of said cell, and allowing hydrogen ions to migrate to the cathode section, and forming water at the cathode; (d) removing regenerated aqueous admixture from anode section, and water 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 reactant comprising an oxidizing polyvalent metal chelate of an acid having the formula ##STR5## wherein from two to four of the groups Y are selected from acetic and propionic acid groups; from zero to two of the groups Y are selected from 2-hydroxy ethyl, 2-hydroxy propyl, and ##STR6## wherein X is selected from acetic acid and propionic acid groups; and R is ethylene, propylene or isopropylene or alternatively cyclohexane or benzene where the two hydrogen atoms replaced by nitrogen atoms are in the 1,2 position, 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 said acid; (b) removing sulfur from the 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 the reduced chelate or chelates in the admixture at the anode and producing a regenerated aqueous admixture containing regenerated oxidizing reactant, the anode section and the cathode section of the electrochemical cell being separated by a hydrogen ion permeable barrier; concomitantly supplying oxygen to the cathode section of said cell, and allowing hydrogen ions to migrate to the cathode section, and forming water at the cathode; (d) removing regenerated aqueous admixture from anode section, and water from said cathode section; and (e) returning regenerated aqueous admixture to the contacting zone.

Claim 5

The process of claim 2 wherein the oxidizing reactant is the ferric chelate of N-(2-hydroxyethyl)ethylenediaminetriacetic 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 .