Process for removing carbon dioxide containing acidic gases from gaseous mixtures using aqueous amine scrubbing solutions

Claim 2

In a process for removing CO 2 from gaseous feeds which comprises, in sequential steps: (1) contacting said feed with an aqueous scrubbing solution consisting essentially of an amine and water, at conditions whereby said CO 2 is absorbed in said scrubbing solution, and (2) regenerating said scrubbing solution at conditions whereby said CO 2 is desorbed from said scrubbing solution, the improvement which comprises: providing a sterically hindered amine in said scrubbing solution as at least one of the said amines, and operating said process at conditions whereby the difference between the moles of CO 2 absorbed at the end of step (1) (absorption step) and the moles of CO 2 absorbed at the end of step (2) (desorption step) would be greater at thermodynamic equilibrium of the vapor-liquid system (as determined from the vapor-liquid equilibrium isotherm of the reaction mixture) than in an aqueous amine CO 2 scrubbing process wherein monoethanolamine or diethanolamine is the only amine utilized under similar conditions of gaseous feed composition, scrubbing composition, temperatures and pressures.

Claim 3

The process of claim 1 wherein the sterically hindered amine is a compound containing at least one secondary amino group attached to a secondary or tertiary carbon atom or a primary amino group attached to a tertiary carbon atom and at least one water solubilizing group.

Claim 4

The process of claim 2 wherein the sterically hindered amine is an amino alcohol.

Claim 5

The process of claim 1 wherein the sterically hindered amine is selected from the group consisting of 2-amino-2-methyl-1-propanol, 2-amino-2-methyl-1-butanol, 3-amino-3-methyl-1-butanol, 3-amino-3-methyl-2-butanol, 2-piperidine ethanol, 2-piperidine methanol, 2-methyl piperazine and N 1 (1,1-dimethyl-2-hydroxyethyl)-2-methyl-1,2-propanediamine.

Claim 6

The process of claim 1 wherein the scrubbing solution from step (2) (desorption step) is continuously reused to absorb a feed containing CO 2 .

Claim 7

The process of claim 1 wherein the process is operated at conditions wherein the thermodynamic cyclic capacity would be at least 15% greater than in a process wherein monoethanolamine or diethanolamine is the only amine utilized under similar conditions of gaseous feed composition, scrubbing solution composition, temperatures and pressures.

Claim 8

The process of claim 1 wherein step (1) (absorption step) is carried out at a lower temperature than step (2) (desorption step).

Claim 9

The process of claim 1 wherein said scrubbing solution additionally contains an additive selected from the group consisting of antifoaming agents, antioxidants, corrosion inhibitors and mixtures thereof.

Claim 10

The process of claim 1 wherein said scrubbing solution additionally contains a sterically unhindered amine.

Claim 11

The process of claim 4 wherein the sterically hindered amine is 2-amino-2-methyl-1-propanol.

Claim 12

In a process for substantially completely removing carbon dioxide containing gases from a normally gaseous feed, which comprises, in sequential steps: (1) contacting said feed with an aqueous scrubbing solution consisting essentially of an amine and water, wherein the total amine concentration in said solution is in the range from about 1 to about 6 molar, said contacting being conducted at a temperature ranging from about 20 to about 100° C. and at a pressure ranging from about 5 to about 2000 psig to thereby absorb the carbon dioxide containing acidic gas in said scrubbing solution, and (2) regenerating said scrubbing solution at a temperature in the range from about 50° to about 170° C. and at a pressure ranging from about 1 to about 50 psia to thereby desorb the carbon dioxide containing gases from said scrubbing solution, the improvement which comprises: providing a sterically hindered amino alcohol selected from the group consisting of 2-amino-2-methyl-1-propanol, 2-amino-2-methyl-1-butanol, 3-amino-3-methyl-1-butanol, and 3-amino-3-methyl-2-butanol in said scrubbing solution as at least one of said amines, and operating said process at conditions whereby the difference between the moles of CO 2 absorbed at the end of step (1) (absorption step) and the moles of CO 2 absorbed at the end of step (2) (desorption step) would be at least 15% greater at thermodynamic equilibrium in the system (as determined from the vapor-liquid equilibrium isotherm in the reaction mixture) than in an aqueous amine CO 2 scrubbing process wherein monoethanolamine is the only amine utilized under substantially the same conditions of gaseous feed composition, scrubbing solution composition, temperatures and pressures.

Claim 13

In a process for substantially completely removing carbon dioxide containing gases from a normally gaseous feed, which comprises, in sequential steps: (1) contacting said feed with an aqueous scrubbing solution consisting essentially of an amine and water, wherein the total amine concentration in said solution is in the range from about 1 to about 6 molar, said contacting being conducted at a temperature ranging from about 20 to about 100° C. and at a pressure ranging from about 5 to about 2000 psig to thereby absorb the carbon dioxide containing acidic gas in said scrubbing solution, and (2) regenerating said scrubbing solution at a temperature in the range from about 50° to about 170° C. and at a pressure ranging from about 1 to about 50 psia to thereby desorb the carbon dioxide containing gases from said scrubbing solution, the improvement which comprises: providing a sterically hindered amino alcohol selected from the group consisting of 2-amino-2-methyl-1-propanol, 2-amino-2-methyl-1-butanol, 3-amino-3-methyl-1-butanol, and 3-amino-3-methyl-2-butanol in said scrubbing solution as at least one of said amines, and operating said process at conditions whereby the difference between the moles of CO 2 absorbed at the end of step (1) (absorption step) and the moles of CO 2 absorbed at the end of step (2) (desorption step) would be at least 15% greater at thermodynamic equilibrium in the system (as determined from the vapor-liquid equilibrium isotherm in the reaction mixture) than in an aqueous amine CO 2 scrubbing process wherein monoethanolamine is the only amine utilized under substantially the same conditions of gaseous feed composition, scrubbing solution composition, temperatures and pressures.

Claim 14

The process of claim 11 wherein the scrubbing solution from step (2) (desorption step) is continuously recycled to absorb a feed containing CO 2 .

Claim 15

The process of claim 11 wherein the sterically hindered amino alcohol is 2-amino-2-methyl-1-propanol.

Claim 16

The process of claim 11 wherein the scrubbing solution additionally contains a sterically unhindered amine.

Claim 17

The process of claim 11 wherein said scrubbing solution additionally contains an additive selected from the group consisting of antifoaming agents, antioxidants, corrosion inhibitors and mixtures thereof.

Claim 18

The process of claim 1 wherein the total amine concentration in the aqueous solution is in the range from about 1 to about 6 molar.

Claim 19

The process of claim 1 wherein the total amine concentration in the aqueous solution is in the range from about 3 to about 5 molar.

Claim 20

The process of claim 11 wherein the total amine concentration in the aqueous solution is in the range from about 3 to about 5 molar.

Claim 21

The process of claim 11 wherein said contacting of said feed is conducted at a temperature ranging from 40° to about 60° C. and at a pressure ranging from 200 to about 1000 psig, and said regenerating is conducted at a temperature ranging from about 80° to about 150° C. and at a pressure ranging from about 15 to about 30 psia.