Process for removing acidic gases

Claim 2

In a process for removing acidic gases from a gaseous stream containing the same, wherein said gaseous stream is contacted with an amine promoted alkaline salt scrubbing solution, the improvement comprising the combination of the scrubbing solution with an effective amount of a corrosion inhibitor comprising a mixture of salts of antimony and molybdenum.

Claim 3

The process of claim 1 wherein the weight ratio of the antimony salt to the molybdenum salt ranges between about 0.01:1 and about 5:1.

Claim 4

The process of claim 2 wherein the weight ratio of the antimony salt to the molybdenum salt ranges between about 0.05:1 and about 0.2:1.

Claim 5

The process of claim 2 wherein the antimony salt comprises an alkali metal antimony salt.

Claim 6

The process of claim 4 wherein the alkali metal antimony salt is selected from the group consisting of tartrates and sulfates.

Claim 7

The process of claim 5 wherein the molybdenum salt comprises an alkali metal molybdenum salt.

Claim 8

The process of claim 6 wherein the alkali metal molybdenum salt comprises an alkali metal molybdate.

Claim 9

The process of claim 7 wherein the corrosion inhibitor comprises about 0.01 wt.% to about 6 wt.% of the scrubbing solution.

Claim 10

The process of claim 8 wherein the corrosion inhibitor comprises about 0.05 to about 0.2 wt% of the scrubbing solution.

Claim 11

The process of claim 8 wherein the amine promoted alkaline salt scrubbing solution comprises potassium carbonate.

Claim 12

The process of claim 8 wherein the scrubbing solution further comprises a sterically hindered amine.

Claim 13

The process of claim 10 wherein the alkali metal antimony salt is potassium antimony tartrate.

Claim 14

The process of claim 10 wherein the alkali metal molybdate is sodium molybdate.

Claim 15

The process of claim 11 wherein the sterically hindered amine has the general formula ##STR3## where R is a secondary or tertiary alkyl group and n is the integer 2, 3 or 4.

Claim 16

The process of claim 14 wherein the sterically hindered amine is a sterically hindered diamine selected from the group consisting of N-cyclohexyl-1, 2-ethanediamine; N-cyclohexyl-1, 3-propanediamine; N-cyclohexyl-1, 4-butanediamine; and N-cyclohexyl-1,5 pentanediamine.

Claim 17

The process of claim 15 wherein the absorbing solution further comprises a cosolvent.

Claim 18

The process of claim 16 wherein the diamine is N-cyclohexyl-1,3 propanediamine and the absorbing solution additionally contains an amino acid cosolvent containing 4-8 carbon atoms.

Claim 19

The process of claim 17 wherein the cosolvent is pipecolinic acid.

Claim 20

The process of claim 11 wherein the sterically hindered amine is selected from the group of sterically hindered amines having the structures: ##STR4## wherein R is hydrogen or methyl, and R' and R" are each selected from the group consisting of: (a) substituted or unsubstituted, linear or branched alkyl radicals having one to twenty carbon atoms; or (b) substituted or unsubstituted alkylene radicals together having three to six carbon atoms and combined to form a cyclic ring; or (c) substituted or unsubstituted cyclo-alkyl radicals having from four to eight ring carbon atoms; or (d) substituted or unsubstituted hydroxy-alkyl radicals, linear or branched, having from one to twenty carbon atoms; or (e) substituted or unsubstituted aralkyl radicals having from seven to twenty carbon atoms, and wherein R"' is selected from the group consisting of substituted and unsubstituted linear alkyl radicals having from one to twenty carbon atoms.

Claim 21

The process of claim 19 wherein R is hydrogen, R' and R" are each selected from the group consisting of C 1 -C 3 hydrocarbon radicals, and R"' is a methyl radical.

Claim 22

The process of claim 20 wherein the sterically hindered amine is selected from the group consisting of N-secondary butyl glycine, N-secondary butyl N-methyl glycine, and mixtures thereof.

Claim 23

In a process for removing acidic gases from a gaseous stream containing the same wherein said gaseous stream is contacted with a sterically hindered amine promoted potassium carbonate scrubbing solution, the improvement comprising the combination of the scrubbing solution with about 0.01 wt.% to about 6 wt.% of a corrosion inhibitor comprising a mixture of potassium antimony tartrate and sodium molybdate.

Claim 24

In a process for removing acidic gases from a gaseous stream containing the same wherein said gaseous stream is contacted with a sterically hindered amine promoted potassium carbonate scrubbing solution, the improvement comprising the combination of the scrubbing solution with about 0.01 wt.% to about 6 wt.% of a corrosion inhibitor comprising a mixture of potassium antimony tartrate and sodium molybdate.