Cryogenic air distillation with companded nitrogen refrigeration

Claim 2

A process for cryogenically distilling air to produce at least oxygen in an apparatus comprised of a high pressure rectifier and a low pressure N 2 removal column wherein the improvement comprises: (a) producing the refrigeration required for said process by work-expanding a pressurized stream of nitrogen obtained from said process to a pressure no higher than the approximate pressure of the low pressure N 2 removal column; (b) compressing at least part of said N 2 stream supplied to the expander, said compression step being at approximately ambient temperature; and (c) powering said compression by the work obtained from said expansion step.

Claim 3

Process according to claim 1 further comprising obtaining said N 2 stream being compressed by warming the N 2 discharged from said expander, and directing essentially all of it to said compressor inlet.

Claim 4

Process according to claim 1 further comprising obtaining said N 2 stream being compressed by warming the N 2 discharged from said expander, and directing only part of it to said compressor inlet; cooling said compressor discharge; and adding it to the expander inlet stream.

Claim 5

Process according to claim 1 further comprising obtaining said N 2 stream being compressed by warming a pressurized N 2 stream prior to expansion; and also comprising cooling said compressed stream; and then work-expanding said stream to the approximate LP column pressure.

Claim 6

Process according to claim 1 further comprising obtaining said N 2 stream from the overhead of said high pressure rectifier.

Claim 7

Process according to claim 1 wherein said low pressure N 2 removal column is further comprised of an auxiliary argon rectifying section, and further comprising obtaining said N 2 stream by evaporating liquid N 2 from said HP rectifier, which has been reduced in pressure, by exchanging latent heat with vapor from above at least part of the counter-current contacting section of said argon rectifier.

Claim 8

Process according to claim 1 further comprising providing a separate argon removal column at a pressure lower than said N 2 removal column pressure; and obtaining said N 2 stream by evaporating partially depressurized HP rectifier liquid N 2 by latent heat exchange with vapor from above the feed point of said argon removal column.

Claim 9

Apparatus for obtaining refrigeration from a cold pressurized nitrogen stream comprised of a cold nitrogen expander to produce work and refrigeration and a warm nitrogen compressor powered by said expander, wherein the improvement comprises: (a) a conduit and a means for sensible heat exchange connecting said expander discharge to said compressor inlet; (b) a means for directly discharging said compressor effluent; and (c) a means for partially warming said cold pressurized nitrogen enroute to said expander.

Claim 10

Apparatus for obtaining refrigeration from a cold pressurized nitrogen stream comprised of a cold nitrogen expander to produce work and refrigeration and a warm nitrogen compressor powered by said expander, wherein the improvement comprises: (a) a conduit and a means for sensible heat exchange connecting said expander discharge to said compressor inlet; (b) a means for directly discharging said compressor effluent; and (c) a means for partially warming said cold pressurized nitrogen enroute to said expander.

Claim 11

Apparatus according to claim 8 further comprising: (a) high pressure rectifier; and (b) conduit including means for sensible heat exchange connecting said HP rectifier overhead vapor to said expander inlet.

Claim 12

Apparatus according to claim 8 further comprising: (a) high pressure rectifier; (b) low pressure N 2 removal column including auxiliary argon rectifying section; (c) means for latent heat exchange between partially depressurized HP rectifier overhead liquid N 2 and vapor from the upper portion of said argon rectifier; and (d) conduit including means for sensible heat exchange for connecting said evaporated N 2 to the inlet of said expander.

Claim 13

Apparatus according to claim 8 further comprising: (a) high pressure rectifier; (b) low pressure N 2 removal column; (c) lower pressure argon removal column; (d) means for exchanging latent heat between partially depressurized liquid N 2 from said HP rectifier and vapor from the upper portion of said argon removal column; and (e) conduit including means for sensible heat exchange which conducts said evaporated N 2 to the inlet of said expander.

Claim 14

Apparatus for refrigerating cold nitrogen stream in cryogenic distillation of air compressed of cold nitrogen expander to produce work and refrigeration and warm nitrogen compressor powered by said expander, wherein the improvement comprises: (a) conduit and means for sensible heat exchange connecting said compressor discharge and said expander inlet; (b) conduit and means for sensible heat exchange for warming said expander effluent.

Claim 15

Apparatus for refrigerating cold nitrogen stream in cryogenic distillation of air compressed of cold nitrogen expander to produce work and refrigeration and warm nitrogen compressor powered by said expander, wherein the improvement comprises: (a) conduit and means for sensible heat exchange connecting said compressor discharge and said expander inlet; (b) conduit and means for sensible heat exchange for warming said expander effluent.

Claim 16

Apparatus according to claim 12 further comprising: (a) high pressure rectifier; and (b) conduit including means for sensible heat exchange connecting said HP rectifier overhead vapor to said compressor inlet.

Claim 17

Apparatus according to claim 12 further comprising: (a) high pressure rectifier; (b) low pressure N 2 removal column including auxiliary argon rectifying section; (c) means for latent heat exchange between partially depressurized HP rectifier overhead liquid N 2 and vapor from the upper portion of said argon rectifier; and (d) conduit including means for sensible heat exchange for connecting said evaporated N 2 to the inlet of said compressor.

Claim 18

Apparatus according to claim 12 further comprising: (a) high pressure rectifier; (b) low pressure N 2 removal column; (c) lower pressure argon removal column; (d) means for exchanging latent heat between partially depressurized liquid N 2 from said HP rectifier and vapor from the upper portion of said argon removal column; and (e) conduit including means for sensible heat exchange which conducts said evaporated N 2 to the inlet of said compressor.

Claim 19

Apparatus for cryogenic distillation of air comprised of cold nitrogen expander to produce work and refrigeration and warm nitrogen compressor powered by said expander, wherein the improvement comprises: (a) means for combining a first N 2 stream obtained from said distillation apparatus with a second N 2 stream and routing said combined stream to said cold expander; (b) means for warming said expander discharge to approximately ambient temperature; (c) means for supplying a minor fraction of at least one of said warmed expander N 2 and the exhaust N 2 from said distillation apparatus to said warm compressor; and (d) conduit and means for sensible cooling connecting said compressor discharge to said means for combining.

Claim 20

Apparatus for cryogenic distillation of air comprised of cold nitrogen expander to produce work and refrigeration and warm nitrogen compressor powered by said expander, wherein the improvement comprises: (a) means for combining a first N 2 stream obtained from said distillation apparatus with a second N 2 stream and routing said combined stream to said cold expander; (b) means for warming said expander discharge to approximately ambient temperature; (c) means for supplying a minor fraction of at least one of said warmed expander N 2 and the exhaust N 2 from said distillation apparatus to said warm compressor; and (d) conduit and means for sensible cooling connecting said compressor discharge to said means for combining.

Claim 21

Apparatus according to claim 16 further comprising (a) high pressure rectifier; (b) low pressure N 2 removal column; (c) means for associating the LP column overhead N 2 and the expander discharge N 2 ; and (d) means for sensible warming of the associated N 2 stream to near ambient temperature.

Claim 22

Apparatus according to claim 17 further comprising: conduit including means for sensible heat exchange connecting said HP rectifier overhead vapor to said means for combining.

Claim 23

Apparatus according to claim 17 further comprising: (a) low pressure N 2 removal column including auxiliary argon rectifying section; (b) means for latent heat exchange between partially depressurized HP rectifier overhead liquid N 2 and vapor from the upper portion of said argon rectifier; and (c) conduit including means for sensible heat exchange for connecting said evaporated N 2 to said means for combining.

Claim 24

Apparatus according to claim 17 further comprising: (a) lower pressure argon removal column; (b) means for exchanging latent heat between partially depressurized liquid N 2 from said HP rectifier and vapor from the upper portion of said argon removal column; and (c) conduit including means for sensible heat exchange which conducts said evaporated N 2 to said means for combining.