N-Secondary butyl glycine promoted acid gas scrubbing process

Claim 2

A process for the removal of CO 2 from a gaseous stream containing CO 2 which comprises contacting said gaseous stream (1) in an absorption step with an aqueous absorbing solution comprising (a) a basic alkali metal salt or hydroxide selected from the group consisting of alkali metal bicarbonates, carbonates, hydroxides, borates, phosphates, and their mixtures, and (b) an activator or promoter system for said basic alkali metal salt or hydroxide comprising N-secondary butyl glycine; and (2) in a desorption and regeneration step, desorbing at least a portion of the absorbed CO 2 from said absorbing solution.

Claim 3

The process of claim 1 wherein the basic alkali metal salt or hydroxide is potassium carbonate.

Claim 4

The process of claim 1 wherein the aqueous solution contains 10 to about 40% by weight of said basic alkali metal salt or hydroxide.

Claim 5

The process of claim 1 wherein the aqueous solution contains 2 to about 20% by weight of said N-secondary butyl glycine.

Claim 6

The process of claim 4 wherein the aqueous solution contains 5 to about 15% by weight of said N-secondary butyl glycine.

Claim 7

The process of claim 4 wherein the absorbing solution from the regenerating step is recycled for reuse in the absorption step.

Claim 8

The process of claim 1, 2, 3, 4, 5 or 6 wherein the temperature of the absorbing solution during the absoption step is in the range from about 25° to about 200° C., the pressure in the absorber ranges from about 5 to about 200 psia and the partial pressure of the acid gas components in the feed stream ranges from about 1.0 to about 500 psia, and wherein the temperature of the absorbing solution during the regeneration step ranges from about 25° to about 200° C., and at pressures ranging from about 16 to about 100 psia.

Claim 9

The process of claim 1, 2, 3, 4, 5, or 6 wherein the absorbing solution additionally includes additives selected from the group consisting of antifoaming agents, antioxidants and corrosion inhibitors.

Claim 10

A process for the removal of CO 2 from a gaseous stream containing CO 2 which comprises, in sequential steps, (1) contacting the gaseous stream with an absorbing solution comprising (a) from about 20 to about 30% by weight of potassium carbonate, and (b) an activator or promoter system for the potassium carbonate, comprising from about 5 to about 15% by weight of N-secondary butyl glycine as the sole promoter, (c) the balance of the solution comprising water and additives selected from the group consisting of antifoaming agents, antioxidants and corrosion inhibitors, wherein said contacting is conducted at conditions whereby CO 2 is absorbed in said absorbing solution and the temperature of the absorbing solution is in the range from about 35° to about 150° C., and the pressure in the absorber is in the range from about 100 to about 1500 psig; and (2) regenerating said absorbing solution at conditions whereby CO 2 is desorbed from said absorbing solution, wherein the regeneration takes place at temperatures ranging from about 35° to about 150° C. and at pressures ranging from about 5 to about 100 psig.

Claim 11

A process for the removal of CO 2 from a gaseous stream containing CO 2 which comprises, in sequential steps, (1) contacting the gaseous stream with an absorbing solution comprising (a) from about 20 to about 30% by weight of potassium carbonate, and (b) an activator or promoter system for the potassium carbonate, comprising from about 5 to about 15% by weight of N-secondary butyl glycine as the sole promoter, (c) the balance of the solution comprising water and additives selected from the group consisting of antifoaming agents, antioxidants and corrosion inhibitors, wherein said contacting is conducted at conditions whereby CO 2 is absorbed in said absorbing solution and the temperature of the absorbing solution is in the range from about 35° to about 150° C., and the pressure in the absorber is in the range from about 100 to about 1500 psig; and (2) regenerating said absorbing solution at conditions whereby CO 2 is desorbed from said absorbing solution, wherein the regeneration takes place at temperatures ranging from about 35° to about 150° C. and at pressures ranging from about 5 to about 100 psig.

Claim 12

The process of claim 9 wherein the absorbing solution from the regeneration step is recycled for reuse in the absorption step.

Claim 13

An aqueous acid gas scrubbing composition comprising: (a) 10 to about 40% by weight of an alkali metal salt or hydroxide, (b) 2 to about 20% by weight of the sterically hindered monosubstituted amino acid, N-secondary butyl glycine and (c) the balance, water.

Claim 14

An aqueous acid gas scrubbing composition comprising: (a) 10 to about 40% by weight of an alkali metal salt or hydroxide, (b) 2 to about 20% by weight of the sterically hindered monosubstituted amino acid, N-secondary butyl glycine and (c) the balance, water.

Claim 15

The composition of claim 11 wherein said alkali metal salt or hydroxide is potassium carbonate.

Claim 16

An aqueous acid gas scrubbing composition comprising: (a) 20 to 30% by weight of potassium carbonate, (b) 5 to about 15% by weight of N-secondary butyl glycine, and (c) the balance, water.

Claim 17

An aqueous acid gas scrubbing composition comprising: (a) 20 to 30% by weight of potassium carbonate, (b) 5 to about 15% by weight of N-secondary butyl glycine, and (c) the balance, water.

Claim 18

The composition of claims 11, 12 or 13 wherein the composition additionally includes antifoaming agents, antioxidants and corrosion inhibitors.