Removal of oxalate ion from gas treating solutions

Claim 2

A process for the removal of H 2 S from a sour gaseous stream comprising (a) dividing the sour gaseous stream into a major portion and a minor portion comprising from about 0.01 percent by volume to about 30 percent by volume of the total sour gaseous stream; (b) contacting the major portion in a first contacting zone with an aqueous reaction solution at a temperature below the melting point of sulfur, the mixture comprising an effective amount of oxidizing reactant selected from the group consisting of oxidizing polyvalent metal chelates of nitrilotriacetic acid, and mixtures thereof, to produce a sweet gas stream and an aqueous admixture containing sulfur and reduced reactant; (c) removing aqueous admixture from the contacting zone, and removing solid sulfur from said aqueous admixture; (d) regenerating said aqueous admixture, producing a regenerated oxidizing reactant solution, and returning regenerated oxidizing reactant solution to the contacting zone; (e) removing a bleed stream containing a composition selected from polyvalent metal chelates of nitrilotriacetic acid, and mixtures thereof, and containing decomposition products of said composition including oxalate ion, from one or more loci in or between steps b, c or d; (f) contacting said bleed stream with said minor portion in a second contacting zone to reduce the H 2 S concentration in said gaseous stream, and producing hydrogen ions and sulfur in said bleed stream, concomitantly or subsequently adding a composition capable of providing hydrogen ions in said solution under conditions and in an amount sufficient to precipitate ferrous oxalate, but not remove the bulk of the polyvalent metal chelate or chelates in the bleed stream, and precipitating ferrous oxalate and separating precipitated solid from the bleed stream.

Claim 3

The process of claim 1 wherein the sour gaseous stream is selected from natural gas, a stream derived from the gasification of coal, or a process effluent.

Claim 4

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

Claim 5

A process for the removal of H 2 S from a sour gaesous stream comprising (a) dividing the sour gaseous stream into a major portion and a minor portion comprising from about 0.01 percent by volume to about 30 percent by volume of the total sour gaseous stream; (b) contacting the major portion in a first contacting zone with an aqueous reaction solution at a temperature below the melting point of sulfur, the mixture comprising an effective amount of oxidizing reactant selected from the group consisting of oxidizing polyvalent metal chelates of nitrilotriacetic acid, and mixtures thereof, to produce a sweet gas stream and an aqueous admixture containing sulfur and reduced reactant; (c) removing aqueous admixture from the contacting zone, and regenerating said aqueous admixture, producing a regenerated oxidizing reactant solution containing sulfur; (d) removing sulfur from the regenerated oxidizing reactant solution; and returning regenerated oxidizing reactant solution to the contacting zone; (e) removing a bleed stream containing a composition selected from polyvalent metal chelates of nitrilotriacetic acid, and mixtures thereof, and containing decomposition products of said composition including oxalate ion, from one or more loci in or between steps b, c or d; (f) contacting said bleed stream with said minor portion in a second contacting zone to reduce the H 2 S concentration in said gaseous stream, and producing hydrogen ions and sulfur in said bleed stream, concomitantly or subsequently adding a composition capable of providing hydrogen ions in said solution under conditions and in an amount sufficient to precipitate ferrous oxalate, but not remove the bulk of the polyvalent metal chelate or chelates in the bleed stream, and precipitating ferrous oxalate and separating precipitated solid from the bleed stream.

Claim 6

A process for the removal of H 2 S from a sour gaesous stream comprising (a) dividing the sour gaseous stream into a major portion and a minor portion comprising from about 0.01 percent by volume to about 30 percent by volume of the total sour gaseous stream; (b) contacting the major portion in a first contacting zone with an aqueous reaction solution at a temperature below the melting point of sulfur, the mixture comprising an effective amount of oxidizing reactant selected from the group consisting of oxidizing polyvalent metal chelates of nitrilotriacetic acid, and mixtures thereof, to produce a sweet gas stream and an aqueous admixture containing sulfur and reduced reactant; (c) removing aqueous admixture from the contacting zone, and regenerating said aqueous admixture, producing a regenerated oxidizing reactant solution containing sulfur; (d) removing sulfur from the regenerated oxidizing reactant solution; and returning regenerated oxidizing reactant solution to the contacting zone; (e) removing a bleed stream containing a composition selected from polyvalent metal chelates of nitrilotriacetic acid, and mixtures thereof, and containing decomposition products of said composition including oxalate ion, from one or more loci in or between steps b, c or d; (f) contacting said bleed stream with said minor portion in a second contacting zone to reduce the H 2 S concentration in said gaseous stream, and producing hydrogen ions and sulfur in said bleed stream, concomitantly or subsequently adding a composition capable of providing hydrogen ions in said solution under conditions and in an amount sufficient to precipitate ferrous oxalate, but not remove the bulk of the polyvalent metal chelate or chelates in the bleed stream, and precipitating ferrous oxalate and separating precipitated solid from the bleed stream.

Claim 7

The process of claim 4 wherein the sour gaseous stream is selected from natural gas, a stream derived from the gasification of coal, or a process effluent.

Claim 8

The process of claim 4 wherein the aqueous reaction solution comprises a liquid absorbent selective for CO 2 .