Argon and nitrogen coproduction process

Claim 2

A process for the coproduction of argon and nitrogen from an air stream comprising (i) elevating the pressure of said air stream in a compressor means; (ii) lowering the temperature of the compressed air stream in a first heat exchanger means; (iii) introducing the compressed and cooled air stream into a pressure swing adsorption unit comprising at least two adsorbent beds in order to remove oxygen and to yield a gaseous mixture comprising argon and nitrogen; (iv) separating the argon and nitrogen mixture by cryogenic means.

Claim 3

The process of claim 1, wherein the pressure swing adsorption unit operates at a temperature of 60° F. to -40° F.

Claim 4

The process of claim 1, wherein said adsorbent beds comprise a sieve having a lesser adsorptivity for argon and nitrogen than oxygen.

Claim 5

The process of claim 3, wherein said sieve is carbon molecular sieve.

Claim 6

The process of claim 1, wherein the air stream is compressed to a pressure of 30 to 60 psig.

Claim 7

The process of claim 1, wherein following compression, the compressed air stream is subjected to the removal of water and carbon dioxide.

Claim 8

The process of claim 6, wherein water and carbon dioxide removal occurs in a 13× molecular sieve bed.

Claim 9

The process of claim 7, wherein said molecular sieve bed is regenerated with vent gas from the said pressure swing adsorption unit.

Claim 10

The process of claim 1, comprising periodically regenerating the adsorbent beds of the pressure swing adsorption unit by venting to the atmosphere.

Claim 11

The process of claim 9, wherein subsequent to the atmospheric venting the beds are further regenerated by lowering the bed pressure with a vacuum pump.

Claim 12

The process of claim 9, wherein the vent gas from each of the adsorbent beds is returned through said first heat eschanger means.

Claim 13

The process of claim 1, further comprising introducing said gaseous mixture comprising argon and nitrogen into a second heat exchanger means to provide further cooling.

Claim 14

The process of claim 1, wherein said cryogenic means is a distillation column.

Claim 15

The process of claim 13, wherein said distillation column is refrigerated by a heat-pump fluid stream which is successively passed through a compressor, said first heat exchanger means and a second heat exchanger means, to cool said heat-pump fluid stream.

Claim 16

The process of claim 14, wherein subsequent to passing through said second heat exchanger means a portion of said heat-pump fluid stream is condensed in a third heat exchanger means.

Claim 17

The process of claim 15, wherein the condensed heat-pump fluid is subsequently expanded in a Joule-Thomson means.

Claim 18

The process of claim 15, wherein the remaining portion of the said heat-pump fluid stream exiting said second heat exchanger means is expanded in a turboexpander means to provide further cooling.

Claim 19

The process of claim 17, wherein said heat-pump fluid streams are combined and condensed in the reboiler tubes of said distillation column.

Claim 20

The process of claim 18, wherein the condensed heat-pump stream is passed through a second Joule-Thomson means to expand and further cool said heat-pump fluid.

Claim 21

The process of claim 19, wherein the expanded and cooled heat pump fluid is passed to a condenser, and wherein a portion of the overhead vapor product of said distillation column is condensed in said condenser.

Claim 22

The process of claim 20, wherein subsequent to said condenser, said heat-pump fluid is passed successively through said third, second, and first heat exchanger means to provide refrigeration to other process streams prior to returning to said compressor means.

Claim 23

The process of claim 20, wherein the uncondensed portion of said overhead vapor product of said distillation is passed successively through said third, second and first heat exchanger means to recover its refrigeration.

Claim 24

The process of claim 13, wherein a liquid crude argon product is recovered as bottoms of said distillation column.

Claim 25

A process for the coproduction of argon and nitrogen comprising (i) elevating the pressure of air in a compressor means; (ii) lowering the temperature of the compressed air in a first heat exchanger means; (iii) introducing the compressed and cooled air into a pressure swing adsorption unit comprising at least two adsorbent beds to remove oxygen and to yield a gaseous mixture comprising argon and nitrogen; (iv) introducing said argon and nitrogen mixture from said pressure swing adsorption unit into a second heat exchanger means to further cool said gases; (v) separating the argon and nitrogen mixture in a distillation column; (vi) refrigerating said distillation column with a heat-pump fluid stream which is successively passed through a compressor, said first heat exchanger means, said second heat exchanger means, a first Joule-Thomson means, and a turboexpander means to cool said heat pump stream; (vii) condensing said cooled heat-pump fluid stream in reboiler tubes of said distillation column; (viii) expanding and cooling the heat-pump fluid stream condensate in a second Joule-Thomson means; (ix) passing the heat-pump fluid successively through a third heat exchanger means, said second, and said first heat exchanger means to provide refrigeration prior to returning to said compressor means; and (x) passing the gaseous overhead product from said distillation column through said third, second and first heat exchanger means to recover its refrigeration.

Claim 26

A process for the coproduction of argon and nitrogen comprising (i) elevating the pressure of air in a compressor means; (ii) lowering the temperature of the compressed air in a first heat exchanger means; (iii) introducing the compressed and cooled air into a pressure swing adsorption unit comprising at least two adsorbent beds to remove oxygen and to yield a gaseous mixture comprising argon and nitrogen; (iv) introducing said argon and nitrogen mixture from said pressure swing adsorption unit into a second heat exchanger means to further cool said gases; (v) separating the argon and nitrogen mixture in a distillation column; (vi) refrigerating said distillation column with a heat-pump fluid stream which is successively passed through a compressor, said first heat exchanger means, said second heat exchanger means, a first Joule-Thomson means, and a turboexpander means to cool said heat pump stream; (vii) condensing said cooled heat-pump fluid stream in reboiler tubes of said distillation column; (viii) expanding and cooling the heat-pump fluid stream condensate in a second Joule-Thomson means; (ix) passing the heat-pump fluid successively through a third heat exchanger means, said second, and said first heat exchanger means to provide refrigeration prior to returning to said compressor means; and (x) passing the gaseous overhead product from said distillation column through said third, second and first heat exchanger means to recover its refrigeration.

Claim 27

The process of claim 24, wherein said expanded and cooled heat-pump fluid is passed to a condenser, where a portion of the overhead vapor of said distillation column is condensed.