Process for the removal of oxalate ion from gas treating solutions

Claim 2

A process comprising contacting an aqueous solution containing decomposition products of a polyvalent metal chelate or chelates of nitrilotriacetic acid, including oxalate ion, with an amount of a composition capable of providing hydrogen ions in said solution sufficient to precipitate ferrous oxalate, under conditions to precipitate ferrous oxalate, and precipitating ferrous oxalate and separating precipitated solid from the solution.

Claim 3

The process of claim 1 wherein the aqueous solution is a bleed stream from a process for removing H 2 S from sour gaseous streams in which the H 2 S-containing gaseous stream is contacted with an oxidizing reactant solution containing an effective amount of an oxidizing reactant selected from the group consisting of oxidizing polyvalent metal chelates of nitrilotriacetic acid, and mixtures thereof.

Claim 4

The process of claim 1 wherein the polyvalent metal chelate is an iron chelate of nitrilotriacetic acid.

Claim 5

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

Claim 6

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 mixture comprising an effective amount of an 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; (b) removing aqueous admixture from the contacting zone, and removing solid sulfur from said aqueous admixture; (c) regenerating said aqueous admixture, producing a regenerated oxidizing reactant solution, and returning regenerated oxidizing reactant solution to the contacting zone; (d) 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 a, b, or c; (e) contacting said bleed stream with a sufficient amount of a composition capable of providing hydrogen ions in solution to precipitate ferrous oxalate, under conditions 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

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 mixture comprising an effective amount of an 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; (b) removing aqueous admixture from the contacting zone, and removing solid sulfur from said aqueous admixture; (c) regenerating said aqueous admixture, producing a regenerated oxidizing reactant solution, and returning regenerated oxidizing reactant solution to the contacting zone; (d) 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 a, b, or c; (e) contacting said bleed stream with a sufficient amount of a composition capable of providing hydrogen ions in solution to precipitate ferrous oxalate, under conditions 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 8

The process of claim 5 wherein the oxidizing reactant is the ferric chelate of nitrilotriacetic acid.

Claim 9

The process of claim 6 wherein, after separation of precipitated solid, the pH of the remaining bleed stream is adjusted to a pH of 7 or greater, and at least the bulk of said bleed stream is returned to one or more loci in steps a, b, or c.

Claim 10

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 mixture comprising an effective amount of an 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; (b) removing aqueous admixture form the contacting zone; (c) regenerating aqueous admixture from step (b), producing a regenerated oxidizing reactant solution, and removing solid sulfur from the regenerated oxidizing reactant solution; (d) 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 a, b, c, or d; (f) contacting said bleed stream with a sufficient amount of a composition capable of providing hydrogen ion in solution to precipitate ferrous oxalate, under conditions to precipitate ferrous oxalate, but not remove the bulk of the polyvalent chelate or chelates in the bleed stream, and precipitating ferrous oxalate and separating precipitated solid from the bleed stream.

Claim 11

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 mixture comprising an effective amount of an 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; (b) removing aqueous admixture form the contacting zone; (c) regenerating aqueous admixture from step (b), producing a regenerated oxidizing reactant solution, and removing solid sulfur from the regenerated oxidizing reactant solution; (d) 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 a, b, c, or d; (f) contacting said bleed stream with a sufficient amount of a composition capable of providing hydrogen ion in solution to precipitate ferrous oxalate, under conditions to precipitate ferrous oxalate, but not remove the bulk of the polyvalent chelate or chelates in the bleed stream, and precipitating ferrous oxalate and separating precipitated solid from the bleed stream.

Claim 12

The process of claim 7 wherein the oxidizing reactant is the ferric chelate of nitrilotriacetic acid.

Claim 13

The process of claim 9 wherein, after separation of precipitated solid, the pH of the remaining bleed stream is adjusted to a pH of 7 or greater, and at least the bulk of said bleed stream is returned to one or more loci in steps a, b, c, or d.

Claim 14

The process of claim 7 wherein the aqueous reaction solution comprises a liquid absorbent for CO 2 .

Claim 15

The process of claim 10 wherein the aqueous reaction solution comprises a liquid absorbent for CO 2 .