Removal of H2 S from gas streams

Claim 2

A process for the removal of H 2 S from a sour gaseous stream comprising (a) feeding the sour gaseous stream to a first contacting zone, and intimately contacting the sour gaseous stream in said first contacting zone with an aqueous reactant solution containing solubilized ferric chelate of nitrilotriacetic acid, and solubilized ferrous chelate of nitrilotriacetic acid, at a temperature below the melting point of sulfur, at sufficient solution to gas ratio and conditions effective to convert H 2 S to sulfur and inhibit sulfur deposition, and producing a gas-solution mixture comprising sour gas and aqueous reactant solution; (b) passing gas-solution mixture from step (a) through a plurality of enclosed contacting sections in serial flow communication in a second contacting zone, under conditions to convert H 2 S to sulfur and at a temperature below the melting point of sulfur, the first contacting section of said second contacting zone comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; the second contacting section through which gas-solution mixture is passed comprising an enclosed mixing section adapted to allow radial mixing of gas-solution mixture and redistribution of solution in gas, and to inhibit plugging due to sulfur formation, the third contacting section through which gas-solution mixture is passed comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; and producing a gas-reactant solution mixture containing solid sulfur in said second contacting zone, the reactant solution of said gas-reactant solution mixture having a reduced content of solubilized ferric chelate of nitrilotriacetic acid and the gas of said mixture having a reduced H 2 S content; and (c) separating the gas having reduced H 2 S content from gas-reactant solution mixture produced in step (b).

Claim 3

The process of claim 1 wherein the gas having reduced H 2 S content from step (c) is contacted with additional aqueous reactant solution containing solubilized ferric chelate of nitrilotriacetic acid, at a temperature below the melting point of sulfur and under conditions effective to convert H 2 S to sulfur, in at least one additional contacting zone, and a gas having further reduced H 2 S content and a solution having a reduced content of the solubilized ferric chelate of nitrilotriacetic acid are produced.

Claim 4

The process of claim 2 wherein at least one of said additional contacting zone or zones comprises a spraying zone wherein the gas having reduced H 2 S content is passed countercurrently through a spray of said additional reactant solution.

Claim 5

The process of claim 3 wherein the solution having a reduced content of the ferric chelate of nitrilotriacetic acid and the solution having a reduced content of nitrilotriacetic acid from said additional contacting zone or zones are regenerated in a regeneration zone.

Claim 6

The process of claim 1 wherein the number of contacting sections comprising a plurality of discrete sulfur deposition resistant channels is from 2 to 30, and the number of contacting sections comprising an enclosed mixing section is from 1 to 30, the contacting sections comprising channels and the enclosed mixing sections adapted to allow radial mixing alternating in the sequence of flow of the gas-solution mixture through the second contacting zone.

Claim 7

The process of claim 2 wherein the number of contacting sections comprising a plurality of discrete sulfur deposition resistant channels is from 2 to 30, and the number of contactng sections comprising an enclosed mixing section is from 1 to 30, the contacting sections comprising channels and the enclosed mixing sections adapted to allow radial mixing alternating in the sequence of flow of the gas-solution mixture through the second contacting zone.

Claim 8

The process of claim 3 wherein the number of contacting sections comprising a plurality of discrete sulfur deposition resistant channels is from 2 to 30, and the number of contacting sections comprising an enclosed mixing section is from 1 to 30, the contacting sections comprising channels and the enclosed mixing sections adapted to allow radial mixing alternating in the sequence of flow of the gas-solution mixture through the second contacting zone.

Claim 9

The process of claim 4 wherein the number of contacting sections comprising a plurality of discrete sulfur deposition resistant channels is from 2 to 30, and the number of contacting sections comprising an enclosed mixing section is from 1 to 30, the contacting sections comprising channels and the enclosed mixing sections adapted to allow radial mixing alternating in the sequence of flow of the gas-solution mixture through the second contacting zone.

Claim 10

A process for the removal of H 2 S from a sour gaseous stream comprising (a) feeding the sour gaseous stream to a first contacting zone, and intimately contacting the sour gaseous stream in said first contacting zone with an aqueous reactant solution containing solubilized ferric chelate of nitrilotriacetic acid, and solubilized ferrous chelate of nitrilotriacetic acid, at a temperature below the melting point of sulfur, at sufficient solution to gas ratio and conditions effective to convert H 2 S to sulfur and inhibit sulfur deposition, and producing a gas-solution mixture comprising sour gas and aqueous reactant solution; (b) passing gas-solution mixture from step (a) through a plurality of enclosed contacting sections in serial flow communication in a second contacting zone, under conditions to convert H 2 S to sulfur and at a temperature below the melting point of sulfur, the first contacting section of said second contacting zone comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; the second contacting section through which gas-solution mixture is passed comprising an enclosed mixing section adapted to allow radial mixing of gas-solution mixture and redistribution of solution in gas, and to inhibit plugging due to sulfur formation, the third contacting section through which gas-solution mixture is passed comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; and producing a gas-reactant solution mixture containing solid sulfur in said second contacting zone, the reactant solution of said gas-reactant solution mixture having a reduced content of solubilized ferric chelate of nitrilotriacetic acid and the gas of said mixture having a reduced H 2 S content; (c) separating the gas having reduced H 2 S content from gas-reactant solution mixture produced in step (b), and recovering a spent reactant solution containing sulfur; (d) removing sulfur from said spent reactant solution containing sulfur; (e) regenerating spent reactant solution from which sulfur has been removed, producing a reactant solution having an increased concentration of ferric chelate of nitrilotriacetic acid; and (f) passing regenerated solution from step (e) to the first contacting zone for use as aqueous reactant solution therein.

Claim 11

A process for the removal of H 2 S from a sour gaseous stream comprising (a) feeding the sour gaseous stream to a first contacting zone, and intimately contacting the sour gaseous stream in said first contacting zone with an aqueous reactant solution containing solubilized ferric chelate of nitrilotriacetic acid, and solubilized ferrous chelate of nitrilotriacetic acid, at a temperature below the melting point of sulfur, at sufficient solution to gas ratio and conditions effective to convert H 2 S to sulfur and inhibit sulfur deposition, and producing a gas-solution mixture comprising sour gas and aqueous reactant solution; (b) passing gas-solution mixture from step (a) through a plurality of enclosed contacting sections in serial flow communication in a second contacting zone, under conditions to convert H 2 S to sulfur and at a temperature below the melting point of sulfur, the first contacting section of said second contacting zone comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; the second contacting section through which gas-solution mixture is passed comprising an enclosed mixing section adapted to allow radial mixing of gas-solution mixture and redistribution of solution in gas, and to inhibit plugging due to sulfur formation, the third contacting section through which gas-solution mixture is passed comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; and producing a gas-reactant solution mixture containing solid sulfur in said second contacting zone, the reactant solution of said gas-reactant solution mixture having a reduced content of solubilized ferric chelate of nitrilotriacetic acid and the gas of said mixture having a reduced H 2 S content; (c) separating the gas having reduced H 2 S content from gas-reactant solution mixture produced in step (b), and recovering a spent reactant solution containing sulfur; (d) removing sulfur from said spent reactant solution containing sulfur; (e) regenerating spent reactant solution from which sulfur has been removed, producing a reactant solution having an increased concentration of ferric chelate of nitrilotriacetic acid; and (f) passing regenerated solution from step (e) to the first contacting zone for use as aqueous reactant solution therein.

Claim 12

The process of claim 9 wherein the number of contacting sections comprising a plurality of discrete sulfur deposition resistant channels is from 2 to 30, and the number of contacting sections comprising an enclosed mixing section is from 1 to 30, the contacting sections comprising channels and the enclosed mixing sections adapted to allow radial mixing alternating in the sequence of flow of the gas-solution mixture through the second contacting zone.

Claim 13

A process for the removal of H 2 S from a sour gaseous stream comprising (a) feeding the sour gaseous stream to a first contacting zone, and intimately contacting the sour gaseous stream in said first contacting zone with an aqueous reactant solution containing solubilized ferric chelate of nitrilotriacetic acid, and solubilized ferrous chelate of nitrilotriacetic acid, at a temperature below the melting point of sulfur, and at sufficient solution to gas ratio and conditions effective to convert H 2 S to sulfur and inhibit sulfur deposition, and producing a gas-solution mixture comprising sour gas and aqueous reactant solution; (b) passing gas-solution mixture from step (a) through a plurality of enclosed contacting sections in serial flow communication in a second contacting zone, under conditions to convert H 2 S to sulfur and at a temperature below the melting point of sulfur, the first contacting section of said second contacting zone comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; the second contacting section through which gas-solution mixture is passed comprising an enclosed mixing section adapted to allow radial mixing of gas-solution mixture and redistribution of solution in gas, and to inhibit plugging due to sulfur formation, the third contacting section through which gas-solution mixture is passed comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; and producing a gas-reactant solution mixture containing solid sulfur in said second contacting zone, the reactant solution of said gas-reactant solution mixture having a reduced content of solubilized ferric chelate of nitrilotriacetic acid and the gas of said mixture having a reduced H 2 S content; (c) separating the gas having reduced H 2 S content from gas-reactant solution mixture produced in step (b), and recovering a spent reactant solution containing sulfur; (d) regenerating spent reactant solution, producing a regenerated solution containing sulfur and having an increased concentration of ferric chelate of nitrilotriacetic acid; (e) removing sulfur from said regenerated solution containing sulfur; and (f) passing regenerated solution from which sulfur has been removed from step (e) to the first contacting zone for use as aqueous reactant solution therein.

Claim 14

A process for the removal of H 2 S from a sour gaseous stream comprising (a) feeding the sour gaseous stream to a first contacting zone, and intimately contacting the sour gaseous stream in said first contacting zone with an aqueous reactant solution containing solubilized ferric chelate of nitrilotriacetic acid, and solubilized ferrous chelate of nitrilotriacetic acid, at a temperature below the melting point of sulfur, and at sufficient solution to gas ratio and conditions effective to convert H 2 S to sulfur and inhibit sulfur deposition, and producing a gas-solution mixture comprising sour gas and aqueous reactant solution; (b) passing gas-solution mixture from step (a) through a plurality of enclosed contacting sections in serial flow communication in a second contacting zone, under conditions to convert H 2 S to sulfur and at a temperature below the melting point of sulfur, the first contacting section of said second contacting zone comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; the second contacting section through which gas-solution mixture is passed comprising an enclosed mixing section adapted to allow radial mixing of gas-solution mixture and redistribution of solution in gas, and to inhibit plugging due to sulfur formation, the third contacting section through which gas-solution mixture is passed comprising a plurality of discrete sulfur deposition resistant channels, each discrete channel providing a diverted flow path for gas-solution mixture through the section, such that gas-solution mixture is directed at least initially at an angle acute to that of the direction of flow of the gas-solution mixture entering the section; and producing a gas-reactant solution mixture containing solid sulfur in said second contacting zone, the reactant solution of said gas-reactant solution mixture having a reduced content of solubilized ferric chelate of nitrilotriacetic acid and the gas of said mixture having a reduced H 2 S content; (c) separating the gas having reduced H 2 S content from gas-reactant solution mixture produced in step (b), and recovering a spent reactant solution containing sulfur; (d) regenerating spent reactant solution, producing a regenerated solution containing sulfur and having an increased concentration of ferric chelate of nitrilotriacetic acid; (e) removing sulfur from said regenerated solution containing sulfur; and (f) passing regenerated solution from which sulfur has been removed from step (e) to the first contacting zone for use as aqueous reactant solution therein.

Claim 15

The process of claim 11 wherein the number of contacting sections comprising a plurality of discrete sulfur deposition resistant channels is from 2 to 30, and the number of contacting sections comprising an enclosed mixing section is from 1 to 30, the contacting sections comprising channels and the enclosed mixing sections adapted to allow radial mixing alternating in the sequence of flow of the gas-solution mixture through the second contacting zone.

Claim 16

The process of claim 1 wherein the solubilized ferric chelate is ammonium ferric nitrilotriacetate chelate and the solubilized ferrous chelate is ammonium ferrous nitrilotriacetate chelate.

Claim 17

The process of claim 2 wherein the solubilized ferric chelate is ammonium ferric nitrilotriacetate chelate and the solubilized ferrous chelate is ammonium ferrous nitrilotriacetate chelate.

Claim 18

The process of claim 9 wherein the solubilized ferric chelate is ammonium ferric nitrilotriacetate chelate and the solubilized ferrous chelate is ammonium ferrous nitrilotriacetate chelate.

Claim 19

The process of claim 11 wherein the solubilized ferric chelate is ammonium ferric nitrilotriacetate chelate and the solubilized ferrous chelate is ammonium ferrous nitrilotriacetate chelate.

Claim 20

The process of claim 6 wherein the solubilized ferric chelate is ammonium ferric nitrilotriacetate chelate and the solubilized ferrous chelate is ammonium ferrous nitrilotriacetate chelate.

Claim 21

The process of claim 10 wherein the solubilized ferric chelate is ammonium ferric nitrilotriacetate chelate and the solubilized ferrous chelate is ammonium ferrous nitrilotriacetate chelate.

Claim 22

The process of claim 12 wherein the solubilized ferric chelate is ammonium ferric nitrilotriacetate chelate and the solubilized ferrous chelate is ammonium ferrous nitrilotriacetate chelate.