Extraction process

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 mixture comprising an effective amount of a reactant selected from the group consisting of polyvalent metallic ions and polyvalent metal chelate compounds, 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; (c) contacting said aqueous admixture in an extraction zone with a liquid composition selected from compounds having the formula C n H 2n+1 OH, wherein n is a number from 4 through 15, and mixtures thereof, in an amount sufficient to remove at least the bulk of the sulfur from said aqueous admixture and produce a separate liquid layer containing sulfur and said composition, and forming a three phase mass comprising an upper liquid layer comprising solid sulfur and said composition, and a lower layer in contact with said upper layer, said lower layer comprising aqueous admixture; (d) separating at least a portion of the upper liquid layer, and recovering sulfur from the portion separated; (e) separating aqueous admixture from the lower layer, and regenerating separated aqueous admixture in a regeneration zone to produce an aqueous admixture containing a regenerated reactant; (f) returning aqueous admixture from the regeneration zone to the contacting zone.

Claim 3

The process of claim 1 wherein at least a portion of the upper liquid layer separated in step (d) is, after sulfur removal, returned to the extraction zone.

Claim 4

The process of claim 2 wherein the reactant is the Fe(III) chelate of nitrilotriacetic acid.

Claim 5

The process of claim 2 wherein the reactant is the Fe(III) chelate of N-(2-hydroxyethyl)ethylenediamine triacetic 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 a reactant selected from the group consisting of polyvalent metallic ions and polyvalent metal chelate compounds, 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 regenerating the aqueous admixture to produce a regenerated aqueous admixture containing a regenerated reactant and sulfur; (c) contacting regenerated liquid aqueous admixture in an extraction zone with a liquid composition selected from compound having the formula C n H 2n+1 OH, wherein n is a whole number from 4 through 15, and mixtures thereof, in an amount sufficient to remove at least the bulk of the sulfur from said regenerated aqueous admixture and produce a separate liquid layer containing sulfur and said composition, and forming a three phase mass comprising an upper liquid layer comprising solid sulfur and said composition, and a lower layer in contact with said upper layer, said lower layer comprising regenerated aqueous admixture; (d) separated at least a portion of the upper layer, and recovering sulfur from the portion separated; (e) separating regenerated aqueous admixture from the lower layer, and returning regenerated aqueous admixture from the extraction zone to the contacting zone.

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 a reactant selected from the group consisting of polyvalent metallic ions and polyvalent metal chelate compounds, 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 regenerating the aqueous admixture to produce a regenerated aqueous admixture containing a regenerated reactant and sulfur; (c) contacting regenerated liquid aqueous admixture in an extraction zone with a liquid composition selected from compound having the formula C n H 2n+1 OH, wherein n is a whole number from 4 through 15, and mixtures thereof, in an amount sufficient to remove at least the bulk of the sulfur from said regenerated aqueous admixture and produce a separate liquid layer containing sulfur and said composition, and forming a three phase mass comprising an upper liquid layer comprising solid sulfur and said composition, and a lower layer in contact with said upper layer, said lower layer comprising regenerated aqueous admixture; (d) separated at least a portion of the upper layer, and recovering sulfur from the portion separated; (e) separating regenerated aqueous admixture from the lower layer, and returning regenerated aqueous admixture from the extraction zone to the contacting zone.

Claim 8

The process of claim 5 wherein at least a portion of the upper liquid layer separated in step (d) is, after sulfur removal, returned to the extraction zone.

Claim 9

The process of claim 5 wherein the reactant is the Fe(III) chelate of nitrilotriacetic acid.

Claim 10

The process of claim 5 wherein the reactant is the Fe(III) chelate of N-(2-hydroxyethyl)ethylenediamine triacetic acid.

Claim 11

The process of claim 1 wherein the extracting composition is a compound having the formula C n H 2n+1 OH, wherein n is a whole number from 10 through 14, and mixtures of such compounds.

Claim 12

The process of claim 5 wherein the extracting composition is a compound having the formula C n H 2n+1 OH, wherein n is a whole number from 10 through 14, and mixtures of such compounds.

Claim 13

The process of claim 9 wherein the reactant is the Fe(III) chelate of N-(2-hydroxyethyl)ethylenediamine triacetic acid.

Claim 14

The process of claim 10 wherein the reactant is the Fe(III) chelate of nitrilotriacetic acid.

Claim 15

The process of any of the preceding claims wherein the sulfur is recovered from the portion separated by melting.