Process for separation and recovery of carbon monoxide

Claim 2

A process for the separation of carbon monoxide from a gas mixture containing same which comprises contacting said gas mixture in a contacting zone with an absorbent consisting essentially of an inert diluent and at least one copper (I) salt selected from the group consisting of: a. the copper (I) salt of an alkane sulfonic acid having from 4 to 20 carbon atoms per molecule; b. the copper (I) salt of an aromatic sulfonic acid having from 6 to 22 carbon atoms per molecule; c. the copper (I) salt of a petroleum sulfonic acid; and d. the copper (I) salt of a dialkyl phosphate having from 1 to 12 carbon atoms per alkyl member, said copper (I) salt being present in said diluent in an amount sufficient to complex at least a portion of said carbon monoxide in said gas mixture, and said diluent being a normally liquid hydrocarbon having a boiling point in the range of 60°-150° C.

Claim 3

The process of claim 1 wherein said carbon monoxide is subsequently separated from the resulting CO/absorbent mixture.

Claim 4

The process of claim 1 wherein said salt is the copper (I) salt of 2-ethyl-1-hexanesulfonic acid.

Claim 5

The process of claim 1 wherein said salt is the copper (I) salt of heptanesulfonic acid.

Claim 6

The process of claim 1 wherein said salt is the copper (I) salt of pentanesulfonic acid.

Claim 7

The process of claim 1 wherein said salt is the copper (I) salt of hexanesulfonic acid.

Claim 8

The process of claim 1 wherein said salt is the copper (I) salt of butanesulfonic acid.

Claim 9

The process of claim 1 wherein said salt is the copper (I) salt of p-dodecylbenzenesulfonic acid.

Claim 10

The process of claim 1 wherein said salt is the copper (I) salt of p-phenolsulfonic acid.

Claim 11

The process of claim 1 wherein said salt is the copper (I) salt of p-toluenesulfonic acid.

Claim 12

The process of claim 1 wherein said salt is the copper (I) salt of naphthalenesulfonic acid.

Claim 13

The purposess of claim 1 wherein said salt is the copper (I) salt of p-chlorobenzenesulfonic acid.

Claim 14

The process of claim 1 wherein said salt is the copper (I) salt of a petroleum sulfonic acid.

Claim 15

The process of claim 1 wherein said copper (I) salt is present in said diluent in an amount ranging from 0.1 to 2 moles per liter of said diluent.

Claim 16

The process of claim 1 wherein said gas mixture is contacted with said absorbent at a temperature in the approximate range of 0° to 25° C below the boiling point of said diluent.

Claim 17

The process of claim 2 wherein said carbon monoxide is liberated from said CO/absorbent mixture by heating same to a temperature in the approximate range of 10° C below the boiling point of said diluent to the boiling point of said diluent.

Claim 18

The process of claim 15 wherein said gas mixture is contacted with said absorbent at a carbon monoxide partial pressure in the range of 0.1 to 20 atmospheres.

Claim 19

A process in accordance with claim 2 wherein said gas mixture consists essentially of carbon monoxide and nitrogen which comprises the steps of: a. passing said mixture to an absorption zone wherein said mixture is contacted with said absorbent; b. withdrawing from said absorption zone a first stream consisting essentially of nitrogen; c. withdrawing from said absorption zone a second stream consisting essentially of said carbon monoxide and said absorbent; d. passing said second stream to a desorption zone wherein said carbon monoxide is desorbed from said absorbent; e. withdrawing from said desorption zone a third stream consisting essentially of carbon monoxide; f. withdrawing from said desorption zone a fourth stream consisting essentially of said absorbent; g. recycling said fourth stream to said absorption zone; h. passing said first stream to a work recovery zone wherein said stream is cooled and mechanical energy is obtained; and i. withdrawing from said work recovery zone a fifth stream consisting essentially of cooled nitrogen.

Claim 20

The process of claim 18 wherein said third stream additionally contains a minor amount of said diluent in the gaseous form which additionally comprises passing said third stream through a heat exchanger, wherein said stream is cooled and at least a portion of said diluent is condensed, and thence to a separator and separately withdrawing from said separator a sixth stream consisting essentially of carbon monoxide and a seventh stream consisting essentially of said diluent.

Claim 21

The process of claim 19 which additionally comprises passing said sixth stream to a compressing zone wherein said carbon monoxide is compressed to obtain an eighth stream consisting essentially of compressed carbon monoxide.

Claim 22

The process of claim 20 which additionally comprises passing said eighth stream through a heat exchanger to cool same and wherein said fifth stream is employed to cool said eighth stream.

Claim 23

The process of claim 20 wherein at least a portion of said mechanical energy from said work recovery zone is employed to compress said sixth stream.