Increased argon recovery from air distillation

Claim 2

In a process for producing high purity oxygen and by-product argon by distilling cooled and cleaned air in a distillation apparatus comprised of a high pressure (HP) rectifier and a low pressure (LP) column comprised of an argon stripping section, a nitrogen removal section, and an argon rectifying section, the improvement comprising: exchanging latent heat between the argon rectifying section and the nitrogen removal section so as to provide intermediate reflux to the former and intermediate reboil to an intermediate height of the latter.

Claim 3

The process according to claim 1 further comprising directing feed fluid derived from at least part of HP rectifier bottom product to said N 2 removal section at a height above said intermediate reboil height.

Claim 4

The process according to claim 2 further comprising providing refrigeration by work expanding at least one of part of the supply air and part of the HP rectifier vapor; and evaporating pressurized argon stripper liquid oxygen bottom product by latent heat exchange with a totally condensing minor fraction of said supply air.

Claim 5

Process according to claim 3 further comprising dividing said condensed air into two streams and injecting them into intermediate heights of said HP rectifier and said N 2 removal section respectively as intermediate refluxes therefor.

Claim 6

The process according to claim 1 further comprising partially depressurizing liquid nitrogen (LN 2 ) overhead product from the HP rectifier, refluxing at least part of the argon stripping section of the low pressure column with a condensate obtained by exchanging latent heat with said partially depressurized LN 2 ; and work expanding the resulting gaseous partially depressurized N 2 .

Claim 7

The process according to claim 5 further comprising obtaining the vapor for said exchange of latent heat with depressurized N 2 from an intermediate height of said argon rectifying section; and returning said condensate to an intermediate height of said argon rectifying section, whereby additional reboil and reflux passes through the lower portion of the argon rectifying section.

Claim 8

The process according to claim 1 further comprising partially work expanding a pressurized air stream; condensing said partially expanded stream by latent heat exchange with evaporating liquid from said LP column; and supplying the resulting condensate as reflux to the N 2 removal section.

Claim 9

The process according to claim 5 further comprising condensing a partially work expanded nitrogen containing gaseous stream from the HP rectifier so as to provide intermediate reboil to the LP column, and refluxing the LP column with the resulting condensate.

Claim 10

In a cryogenic air distillation apparatus for producing high purity oxygen plus byproduct argon comprised of a high pressure (HP) rectifier and a low pressure (LP) column comprised of an argon stripping section, a nitrogen removal section, and an argon rectifying section, the improvement comprising: means for exchanging latent heat from an intermediate height of the argon rectifying section to an intermediate height of the nitrogen removal section.

Claim 11

In a cryogenic air distillation apparatus for producing high purity oxygen plus byproduct argon comprised of a high pressure (HP) rectifier and a low pressure (LP) column comprised of an argon stripping section, a nitrogen removal section, and an argon rectifying section, the improvement comprising: means for exchanging latent heat from an intermediate height of the argon rectifying section to an intermediate height of the nitrogen removal section.

Claim 12

The apparatus according to claim 9 further comprised of means for exchanging latent heat between partially depressurized liquid overhead product from said HP rectifier and intermediate height vapor of said LP column; and means for work expanding the resulting evaporated liquid.

Claim 13

A process for producing high purity oxygen and byproduct argon by distilling air in a distillation apparatus comprised of a high pressure (HP) rectifier and a low pressure (LP) column comprised of an argon stripping section a nitrogen removal section, and an argon rectifying section, wherein the improvement comprises: a. partially expanding liquid nitrogen from the HP rectifier overhead; b. evaporating said partially expanded liquid nitrogen by exchanging latent heat with argon rectifying section intermediate height vapor; c. refluxing the argon rectifier with the liquefied intermediate height vapor; and d. work expanding said evaporated partially expanded nitrogen.

Claim 14

A process for producing high purity oxygen and byproduct argon by distilling air in a distillation apparatus comprised of a high pressure (HP) rectifier and a low pressure (LP) column comprised of an argon stripping section a nitrogen removal section, and an argon rectifying section, wherein the improvement comprises: a. partially expanding liquid nitrogen from the HP rectifier overhead; b. evaporating said partially expanded liquid nitrogen by exchanging latent heat with argon rectifying section intermediate height vapor; c. refluxing the argon rectifier with the liquefied intermediate height vapor; and d. work expanding said evaporated partially expanded nitrogen.

Claim 15

The process according to claim 11 further comprising locating said argon rectifying section intermediate height at least two theoretical stages above the bottom of said section.

Claim 16

The process according to claim 11 further comprising: evaporating essentially all of the liquid high purity oxygen bottom product from the low pressure column at a pressure greater than the bottom pressure of the LP column by exchanging latent heat with and condensing a fraction of the cooled and cleaned supply air; and injecting at least part of the resulting condensed air into the N 2 removal section at an intermediate height as intermediate reflux therefor.

Claim 17

Process according to claim 13 further comprising injecting a remaining part of said condensed air into the HP rectifier at an intermediate height as intermediate reflux therefor.

Claim 18

The process according to claim 11 further comprising: evaporating at least part of the liquid high purity oxygen bottom product from the LP column at a pressure higher than the LP column bottom pressure by latent heat exchange with at least a major fraction of partially condensing cooled and cleaned supply air.

Claim 19

The process according to claim 11 further comprising separately exchanging latent heat between a second intermediate height of the argon rectifying section which may be the same as said first intermediate height and an intermediate height of the nitrogen removal section, thereby providing intermediate reboil to the nitrogen removal section and a second source of intermediate reflux to the argon rectifying section.

Claim 20

The process according to claim 11 further comprising partially work expanding a pressurized nitrogen containing gaseous stream from the HP rectifier; condensing said partially expanded stream by latent heat exchange with evaporating intermediate height liquid from the N 2 removal section; and directly injecting the resulting condensate into the N 2 removal section as reflux therefor.

Claim 21

Apparatus for producing oxygen and argon comprised of a low pressure column which includes a nitrogen removal section and an argon rectifying section wherein the improvement comprises means for increasing argon recovery comprised of (a) a first latent heat exchanger in which intermediate height liquid from the N 2 removal section is evaporated and intermediate height vapor from the argon rectifier is condensed; and/or (b) a second latent heat exchanger in which intermediate vapor from the argon rectifier is condensed and liquid nitrogen is evaporated at an intermediate pressure and a work expander for said evaporated intermediate pressure nitrogen.

Claim 22

Apparatus for producing oxygen and argon comprised of a low pressure column which includes a nitrogen removal section and an argon rectifying section wherein the improvement comprises means for increasing argon recovery comprised of (a) a first latent heat exchanger in which intermediate height liquid from the N 2 removal section is evaporated and intermediate height vapor from the argon rectifier is condensed; and/or (b) a second latent heat exchanger in which intermediate vapor from the argon rectifier is condensed and liquid nitrogen is evaporated at an intermediate pressure and a work expander for said evaporated intermediate pressure nitrogen.

Claim 23

Apparatus according to claim 18 further comprised of a latent heat exchanger in which condensing N 2 containing gas provides intermediate reboil to the N 2 removal section, and an expander which discharges said N 2 containing gas.