Production of ultra-high purity oxygen from cryogenic air separation plants

Claim 2

In a process for the fractionation of air by cryogenic distillation using a thermally integrated dual-column cryogenic distillation system comprising a high pressure distillation column and a low pressure distillation column, wherein a feed air stream is compressed, cooled to near its dew point and fed to the high distillation column system for rectification thereby producing a nitrogen containing overhead and a crude liquid oxygen bottoms and wherein the crude liquid oxygen is reduced in pressure, fed to and further fractionated in the low pressure distillation column thereby producing a low pressure nitrogen overhead, the improvement for producing an ultra-high purity oxygen product comprising the steps of: removing an oxygen-containing stream from a location of the thermally integrated dual-column cryogenic distillation system where the removed stream is essentially free of heavier contaminants comprising hydrocarbons, carbon dioxide, xenon and krypton, and subsequently stripping the removed oxygen-containing stream in a cryogenic stripping/distillation column thereby producing an ultra-high purity oxygen product at the bottom of the cryogenic stripping/distillation column.

Claim 3

The process according to claim 1, wherein the removed oxygen-containing stream to be stripped is removed as a liquid stream.

Claim 4

The process according to claim 1, wherein the removed oxygen-containing stream to be stripped is removed as a vapor stream.

Claim 5

The process according to claim 1, wherein the removed oxygen-containing stream to be stripped is removed from the low pressure column.

Claim 6

The process according to claim 1, wherein the removed oxygen-containing stream to be stripped is removed from the high pressure column.

Claim 7

The process according to claim 1, wherein heat duty to provide reboil to the cryogenic stripping/distillation column is provided by at least partially condensing a portion of the nitrogen overhead from the distillation column of the cryogenic distillation system.

Claim 8

In a process for the fractionation of air by cryogenic distillation using a cryogenic distillation column system comprising a high pressure distillation column and a low pressure distillation column, which comprise a dual-column portion of the cryogenic distillation column system, and an argon side-arm distillation column, wherein a feed air stream is compressed, cooled to near its dew point and fed to the high pressure distillation column system for rectification thereby producing a nitrogen containing overhead and a crude liquid oxygen bottoms; wherein the crude liquid oxygen is reduced in pressure, fed to and further fractionated in the low pressure distillation column thereby producing a low pressure nitrogen overhead; and wherein an argon-containing side stream is removed from the low pressure column and rectified in the argon side-arm distillation column thereby producing a crude argon overhead and an enriched oxygen liquid which is returned to the low pressure column, the improvement for producing an ultra-high purity oxygen product comprising the steps of: removing an oxygen-containing stream from a location of the dual-column portion of the cryogenic distillation column system where the removed stream is essentially free of heavier contaminants comprising hydrocarbons, carbon dioxide, xenon and krypton, and subsequently stripping the removed oxygen-containing stream in a cryogenic stripping/distillation column thereby producing an ultra-high purity oxygen product at the bottom of the cryogenic stripping/distillation column.

Claim 9

In a process for the fractionation of air by cryogenic distillation using a cryogenic distillation column system comprising a high pressure distillation column and a low pressure distillation column, which comprise a dual-column portion of the cryogenic distillation column system, and an argon side-arm distillation column, wherein a feed air stream is compressed, cooled to near its dew point and fed to the high pressure distillation column system for rectification thereby producing a nitrogen containing overhead and a crude liquid oxygen bottoms; wherein the crude liquid oxygen is reduced in pressure, fed to and further fractionated in the low pressure distillation column thereby producing a low pressure nitrogen overhead; and wherein an argon-containing side stream is removed from the low pressure column and rectified in the argon side-arm distillation column thereby producing a crude argon overhead and an enriched oxygen liquid which is returned to the low pressure column, the improvement for producing an ultra-high purity oxygen product comprising the steps of: removing an oxygen-containing stream from a location of the dual-column portion of the cryogenic distillation column system where the removed stream is essentially free of heavier contaminants comprising hydrocarbons, carbon dioxide, xenon and krypton, and subsequently stripping the removed oxygen-containing stream in a cryogenic stripping/distillation column thereby producing an ultra-high purity oxygen product at the bottom of the cryogenic stripping/distillation column.

Claim 10

The process according to claim 7, wherein the removed oxygen-containing stream to be stripped is removed as a liquid stream.

Claim 11

The process according to claim 7, wherein the removed oxygen-containing stream to be stripped is removed as a vapor stream.

Claim 12

The process according to claim 7, wherein the removed oxygen-containing stream to be stripped is removed from the low pressure column.

Claim 13

The process according to claim 7, wherein the removed oxygen-containing stream to be stripped is removed from the high pressure column.

Claim 14

The process according to claim 7, wherein the removed oxygen-containing stream to be stripped is removed from the argon side-arm column.

Claim 15

The process according to claim 7, wherein heat duty to provide reboil to the cryogenic stripping/distillation column is provided by at least partially condensing a portion of the nitrogen overhead from the high pressure distillation column of the cryogenic distillation system.

Claim 16

In a process for the fractionation of air by cryogenic distillation using a single (nitrogen generator) distillation column, wherein a feed air stream is compressed, cooled to near its dew point and fed to the distillation column system for rectification thereby producing a nitrogen containing overhead and a crude liquid oxygen bottoms, the improvement for producing an ultra-high purity oxygen product comprising the steps of: rectifying the crude liquid bottoms thereby producing an oxygen-containing stream which is essentially free of heavier contaminants comprising hydrocarbons, carbon dioxide, xenon and krypton, and subsequently stripping the oxygen-containing stream in a cryogenic stripping/distillation column thereby producing an ultra-high purity oxygen product at the bottom of the cryogenic stripping/distillation column, and refluxing said cryogenic stripping/distillation column with a liquid stream from the distillation column which is essentially free of heavier components comprising hydrocarbons, carbon dioxide, xenon and krypton.

Claim 17

In a process for the fractionation of air by cryogenic distillation using a single (nitrogen generator) distillation column, wherein a feed air stream is compressed, cooled to near its dew point and fed to the distillation column system for rectification thereby producing a nitrogen containing overhead and a crude liquid oxygen bottoms, the improvement for producing an ultra-high purity oxygen product comprising the steps of: rectifying the crude liquid bottoms thereby producing an oxygen-containing stream which is essentially free of heavier contaminants comprising hydrocarbons, carbon dioxide, xenon and krypton, and subsequently stripping the oxygen-containing stream in a cryogenic stripping/distillation column thereby producing an ultra-high purity oxygen product at the bottom of the cryogenic stripping/distillation column, and refluxing said cryogenic stripping/distillation column with a liquid stream from the distillation column which is essentially free of heavier components comprising hydrocarbons, carbon dioxide, xenon and krypton.

Claim 18

The process according to claim 14, wherein heat duty to provide reboil to the cryogenic stripping/distillation column is provided by condensing at least a portion of the oxygen-containing stream prior to rectification.

Claim 19

In a process for the fractionation of air by cryogenic distillation using a cryogenic distillation column system comprising a high pressure distillation column, a low pressure distillation column and an argon side-arm distillation column, wherein a feed air stream is compressed, cooled to near its dew point and fed to the high pressure distillation column system for rectification thereby producing a nitrogen containing overhead and a crude liquid oxygen bottoms; wherein the crude liquid oxygen is reduced in pressure, fed to and further fractionated in the low pressure distillation column thereby producing a low pressure nitrogen overhead; and wherein an argon-containing side stream is removed from the low pressure column and rectified in the argon side-arm distillation column thereby producing a crude argon overhead and an enriched oxygen liquid which is returned to the low pressure column, the improvement for producing an ultra-high purity oxygen product comprising the steps of: rectifying the argon-containing side stream to remove heavy comtaminants comprising hydrocarbons, carbon dioxide, xenon and krypton prior to rectification in the argon side-arm distillation and subsequently stripping the produced enriched oxygen liquid thereby producing an ultra-high purity oxygen product.

Claim 20

In a process for the fractionation of air by cryogenic distillation using a cryogenic distillation column system comprising a high pressure distillation column, a low pressure distillation column and an argon side-arm distillation column, wherein a feed air stream is compressed, cooled to near its dew point and fed to the high pressure distillation column system for rectification thereby producing a nitrogen containing overhead and a crude liquid oxygen bottoms; wherein the crude liquid oxygen is reduced in pressure, fed to and further fractionated in the low pressure distillation column thereby producing a low pressure nitrogen overhead; and wherein an argon-containing side stream is removed from the low pressure column and rectified in the argon side-arm distillation column thereby producing a crude argon overhead and an enriched oxygen liquid which is returned to the low pressure column, the improvement for producing an ultra-high purity oxygen product comprising the steps of: rectifying the argon-containing side stream to remove heavy comtaminants comprising hydrocarbons, carbon dioxide, xenon and krypton prior to rectification in the argon side-arm distillation and subsequently stripping the produced enriched oxygen liquid thereby producing an ultra-high purity oxygen product.