Process for separation of gas mixture

Claim 2

In a process for the purification of the low-boiling constituents of a compressed gas mixture from a variable source by cooling to low temperatures in cyclical alternated regenerators to condense high-boiling constituents of said gas mixture comprising (1) passing said gas mixture through a first regenerator from the warm end to the cold end of the same to cool said gas mixture and to condense said high-boiling constituents of said gas mixture thereby producing a purified gas stream; (2) passing large quantities of a scavenging gas which is at a lower pressure than said gas mixture in said first regenerator through a second regenerator from the cold end to the warm end of the same to clean said second regenerator and to re-evaporate said high-boiling constituents, and (3) passing at least part of said purified gas stream through a third regenerator from the cold end to the warm end of same to re-cool said third regenerator, the improvement comprising compressing and recycling at least part of said scavenging gas which has passed through said second regenerator and has thereby become contaminated with high-boiling impurities through said first regenerator from the warm end to the cold end and repeating the process as defined above.

Claim 3

Process as in claim 1 wherein said scavenging gas is obtained by expanding part of said purified gas stream, and wherein the third regenerator is cooled to the temperature of the first regenerator.

Claim 4

Process as in claim 2 wherein said compressed gas mixture is produced by passing said gas mixture through a compressor.

Claim 5

Process as in claim 3 wherein at least part of said scavenging gas is recycled to the inlet of said compressor.

Claim 6

Process as in claim 4 wherein the amount of gas recycled is automatically regulated to thereby maintain a constant amount of gas passing through said first regenerator.

Claim 7

Process as in claim 1 wherein said second regenerator comprises two separate regenerators, 2A and 2B; and wherein part of the expanded purified gas stream from said first regenerator undergoes further pressure reduction and is passed through regenerator 2A, which is kept at sufficiently low pressure to remove most of said high-boiling constituents; and wherein a different part of said expanded purified gas stream is passed through regenerator 2B, which is kept at a pressure above that of regenerator 2A and below that of the first regenerator, to thereby remove substantially all of the balance of said high boiling constituents.

Claim 8

Process as in claim 6 wherein the amount of scavenging gas recycled is varied to thereby maintain a constant amount of gas passing through said fourth regenerator.

Claim 9

Process as in claim 1 wherein said scavenging gas being recycled is combined with a variable source of gas mixture intended for said first regenerator and wherein the amount of this recycled scavenging gas is varied to thereby maintain a constant amount of gas passing through said first regenerator.

Claim 10

A process for purifying a compressed carbonaceous gas mixture from a variable source by removing certain high-boiling constituents by cooling to low temperatures in cyclical alternated regenerators to condense said high-boiling constituents comprising (1) passing said gas mixture through a first regenerator from the warm end to the cold end of said first regenerator to cool said gas mixture and to condense said high-boiling constituents of said gas mixture thereby producing a purified gas stream, (2) expanding part of said purified gas stream and passing it as a scavenging gas through a second regenerator from the cold end to the warm end of the same to clean said second regenerator and to re-evaporate most of said high-boiling constituents, (3) expanding part of said purified gas stream to a lesser level of expansion than in step (2) and passing it as a scavenger gas through a third regenerator from the cold end to the warm end of the same to clean said third regenerator and to re-evaporate additional said high-boiling constituents not previously re-evaporated in step (2), (4) passing a different part of said purified gas stream through a fourth regenerator from the cold end to the warm end of the same to re-cool said fourth regenerator, and (5) compressing and recycling at least part of said scavenging gas which has passed through the second and third regenerators and has thereby become contaminated with high boiling impurities through said first regenerator and repeating the process as defined above.

Claim 11

A process for purifying a compressed carbonaceous gas mixture from a variable source by removing certain high-boiling constituents by cooling to low temperatures in cyclical alternated regenerators to condense said high-boiling constituents comprising (1) passing said gas mixture through a first regenerator from the warm end to the cold end of said first regenerator to cool said gas mixture and to condense said high-boiling constituents of said gas mixture thereby producing a purified gas stream, (2) expanding part of said purified gas stream and passing it as a scavenging gas through a second regenerator from the cold end to the warm end of the same to clean said second regenerator and to re-evaporate most of said high-boiling constituents, (3) expanding part of said purified gas stream to a lesser level of expansion than in step (2) and passing it as a scavenger gas through a third regenerator from the cold end to the warm end of the same to clean said third regenerator and to re-evaporate additional said high-boiling constituents not previously re-evaporated in step (2), (4) passing a different part of said purified gas stream through a fourth regenerator from the cold end to the warm end of the same to re-cool said fourth regenerator, and (5) compressing and recycling at least part of said scavenging gas which has passed through the second and third regenerators and has thereby become contaminated with high boiling impurities through said first regenerator and repeating the process as defined above.

Claim 12

Process as in claim 9 wherein said purified gas stream coming from said fourth regenerator comprises hydrogen, carbon monoxide, methane, and nitrogen, and less than about 0.05 percent by volume of high boiling constituents.

Claim 13

Process as in claim 9 wherein said purified gas stream passed through said second regenerator comprises a further expansion of part of said purified gas stream expanded to pass through said third regenerator, and wherein said fourth regenerator is re-cooled to the temperature of said first regenerator.

Claim 14

Process as in claim 11 wherein said scavenging gas which has passed through said third regenerator is recycled.

Claim 15

Process as in claim 11 wherein said scavenging gas which has passed through said second regenerator is passed through a recovery system to partially recover the high-boiling constituents from the gas stream and then recycling the partially purified gas stream from said recovery system.

Claim 16

Process as in claim 11 wherein said scavenging gas which has passed through said second regenerator and said third regenerator is recycled.

Claim 17

Process as in claim 11 wherein said scavenging gas being recycled is combined with a variable source of gas mixture intended for said first regenerator and wherein the amount of this recycled scavenging gas is varied to thereby maintain a constant amount of gas passing through said first regenerator.

Claim 18

Process as in claim 11 wherein said regenerators are operated at relatively high pressures.

Claim 19

Process as in claim 11 wherein said regenerators are operated at relatively low pressures.

Claim 20

Process as in claim 11 wherein said high-boiling constituents constitutes between a few parts per million and a majority of said gas mixture entering said first regenerator.

Claim 21

Process as in claim 11 wherein between about five and about fifteen weight percent of said compressed gas mixture comprises said high-boiling constituents.

Claim 22

Process as in claim 11 wherein said gas mixture originates from a coal conversion process.

Claim 23

Process as in claim 20 wherein said gas mixture originates from a coke plant.

Claim 24

Process as in claim 9 wherein said second regenerator is depressurized prior to passing said expanded purified gas stream through the same.

Claim 25

Process as in claim 9 wherein the amount of scavenging gas recycled is varied to thereby maintain a constant amount of gas passing through said fourth regenerator.

Claim 26

Process as in claim 9 wherein said compressed gas mixture is produced by passing said gas mixture though a compressor.

Claim 27

Process as in claim 24 wherein at least part of said scavenging gas is recycled to the inlet of said compressor.

Claim 28

Process as in claim 25 wherein the amount of gas recycled is automatically regulated to thereby maintain a constant amount of gas passing through said first regenerator.