Liquefied gases using an air recycle liquefier

Claim 2

In a process for the cryogenic distillative separation of air by fractionation in a distillation column to produce at least one liquid product stream selected from the group consisting of liquid nitrogen, liquid oxygen and/or liquid argon, the improvement comprising: (a) cooling a feed air stream by appropriate refrigeration to produce at least a portion of the feed air stream as a liquid air stream; (b) condensing a product stream against at least a portion of the liquid air stream by indirect heat exchange thereby vaporizing the liquid air stream to produce a substantially gaseous air stream and a liquid product stream; (c) further processing at least a portion of the substantially gaseous air stream by recycling it to feed air.

Claim 3

The process of claim 1 wherein in step (c) the substantially gaseous air stream is recycled by rewarming at least a portion of the gaseous air stream by indirect heat exchange with process streams, compressing said rewarmed gaseous air stream and recycling said compressed gaseous air stream to the feed air stream.

Claim 4

The process of claim 1 step (b) wherein a reflux stream is condensed to produce a liquid reflux stream by indirect heat exchange with said liquid air stream.

Claim 5

The process of claim 1 step (c) wherein at least a portion of said gaseous air stream is fed without recycle to additional separatory steps to produce a product stream.

Claim 6

A process for the cryogenic distillative separation of air to produce at least a liquid nitrogen product, comprising the steps of: (a) compressing feed air to an elevated pressure and removing water, carbon dioxide and condensibles from the feed air; (b) splitting the feed air into a first split feed stream and a second split feed stream; (c) cooling each split feed stream to a lower temperature by indirect heat exchange against process streams; (d) expanding a first portion of the first split feed stream through a warm expander and recycling at least a first part of the expanded stream to the feed air while providing refrigeration to the feed air by indirect heat exchange; (e) expanding the second split feed stream through a cold expander and using at least a first portion of the expanded stream for a distillation step; (f) recycling a second portion of the expanded second split stream to the feed air while providing refrigeration to the feed air by indirect heat exchange; (g) removing an oxygen-enriched stream from the base of the distillation column; (h) removing a gaseous nitrogen stream from the distillation column and condensing a first portion of the gaseous nitrogen stream against a process stream; (i) condensing a second portion of the gaseous nitrogen stream from the distillation column against at least a part of the second portion of the first split stream by indirect heat exchange to produce a liquid nitrogen product, and (j) recycling at least a part of the second portion of the first split stream to the feed air.

Claim 7

A process for the cryogenic distillative separation of air to produce at least a liquid nitrogen product, comprising the steps of: (a) compressing feed air to an elevated pressure and removing water, carbon dioxide and condensibles from the feed air; (b) splitting the feed air into a first split feed stream and a second split feed stream; (c) cooling each split feed stream to a lower temperature by indirect heat exchange against process streams; (d) expanding a first portion of the first split feed stream through a warm expander and recycling at least a first part of the expanded stream to the feed air while providing refrigeration to the feed air by indirect heat exchange; (e) expanding the second split feed stream through a cold expander and using at least a first portion of the expanded stream for a distillation step; (f) recycling a second portion of the expanded second split stream to the feed air while providing refrigeration to the feed air by indirect heat exchange; (g) removing an oxygen-enriched stream from the base of the distillation column; (h) removing a gaseous nitrogen stream from the distillation column and condensing a first portion of the gaseous nitrogen stream against a process stream; (i) condensing a second portion of the gaseous nitrogen stream from the distillation column against at least a part of the second portion of the first split stream by indirect heat exchange to produce a liquid nitrogen product, and (j) recycling at least a part of the second portion of the first split stream to the feed air.

Claim 8

The process of claim 5 wherein in step (e) at least a portion of the expanded second split feed stream is introduced into the distillation column as feed.

Claim 9

The process of claim 6 wherein in step (h), the first portion of the gaseous nitrogen stream is condensed against an oxygen-enriched stream from the distillation column.

Claim 10

The process of claim 7 wherein the gaseous nitrogen stream of step (h) is removed from the top of the distillation column.

Claim 11

The process of claim 7 wherein the gaseous nitrogen stream of step (h) is removed from a high pressure stage of a two pressure stage distillation column.

Claim 12

The process of claim 5 wherein the distillation column is a two stage column with a high pressure stage and a low pressure stage.

Claim 13

The process of claim 10 wherein the first portion of the second split stream is introduced into the high pressure stage of the distillation column.

Claim 14

The process of claim 10 wherein a second part of the expanded first portion of the first split stream is introduced into the low pressure stage of the distillation column.

Claim 15

The process of claim 10 wherein nitrogen gas formed at the top of the high pressure stage is condensed against oxygen enriched liquid in the base of the low pressure stage, the condensed nitrogen is used as reflux for both the high pressure stage and the low pressure stage, the oxygen-enriched stream from the base of the high pressure stage is introduced into the low pressure stage and oxygen-enriched liquid from the base of the low pressure stage is indirectly heat exchanged with the first portion of the gaseous nitrogen stream from the top of the low pressure stage to produce a gaseous oxygen-enriched product and a nitrogen reflux liquid.

Claim 16

The process of claim 13 wherein the oxygen-enriched liquid, from the base of the low pressure column which is indirectly heat exchanged with the first portion of the gaseous nitrogen stream, is removed in part to a side-arm distillation column and is distilled against a part of the second portion of the first split stream which second portion provides the required boil-up at the bottom of the side-arm column to provide a liquid oxygen product, a gaseous oxygen-enriched stream and a feed to the low pressure stage of the two stage distillation column.

Claim 17

The process of claim 10 wherein a part of the second portion of the first split stream is reduced in pressure and introduced into the high pressure stage of the distillation column.

Claim 18

The process of claim 10 wherein a part of the second portion of the first split stream is cooled against process streams and introduced into the low pressure stage of the distillation column.

Claim 19

The process of claim 10 wherein a part of the second portion of the first split stream is combined with the first portion of the second split stream and the combined stream is introduced into the high pressure stage of the distillation column.

Claim 20

The process of claim 10 wherein a part of the second portion of the first split stream is combined with the second part of the first portion of the first split stream and the combined stream is introduced into the low pressure stage of the distillation column.

Claim 21

The process of claim 10 wherein another part of the second portion of the first split stream is boiled against condensing nitrogen gas from the high pressure stage of the distillation column, the resulting boiled stream is recycled to feed air and the condensed nitrogen is split into nitrogen reflux for the low pressure stage and liquid nitrogen product.

Claim 22

The process of claim 10 wherein the gaseous nitrogen of step (h) is removed from the low pressure stage of a two stage distillation column.

Claim 23

The process of claim 5 wherein the liquid nitrogen product is subcooled against at least a part of the second portion of the first split stream and a vapor portion of the liquid nitrogen product derived after said subcooled product is reduced in pressure and phase separated into a subcooled liquid nitrogen product and a vapor-phase nitrogen stream.

Claim 24

The process of claim 5 wherein a second part of the expanded first portion of the first split stream is introduced as feed into a single pressure stage distillation column.

Claim 25

The process of claim 5 wherein the first portion of the second split stream is used to provide the boil-up at the bottom of a single pressure stage distillation column.

Claim 26

The process of claim 23 wherein the first portion of the second split stream is condensed while providing boil-up in said column and said stream is then subcooled and provides some of the liquefaction duty necessary for the condensation of the gaseous nitrogen stream from the overhead of the distillation column to produce liquid nitrogen product.

Claim 27

The process of claim 5 wherein a part of the second portion of the first split stream is boiled against condensing nitrogen gas from the high pressure stage of the distillation column, the resulting boiled stream is recycled to feed air and the condensed nitrogen is split into nitrogen reflux for the high pressure stage of the distillation column and liquid nitrogen product.

Claim 28

A process for the cryogenic distillative separation of air to produce at least a liquid nitrogen product comprising the steps of: (a) compressing feed air to an elevated pressure and removing water, carbon dioxide and condensibles from the feed air; (b) splitting the feed air into a first split feed stream and a second split feed stream; (c) cooling each split feed stream to a lower temperature by indirect heat exchange against process streams; (d) expanding a first portion of the first split feed stream through a warm expander and recycling a first part of the expanded stream to feed air while providing refrigeration to the feed air by indirect heat exchange; (e) expanding the second split feed stream through a cold expander and introducing a first portion of the expanded stream into a boiler/condenser in the base of a distillation column to provide boil-up in the column and at least partially condense said expanded first portion; (f) cooling and phase separating a second portion of the first split stream and combining the vapor phase of said second portion with said first portion of the expanded stream of step (e) before its introduction into the boiler/condenser; (g) combining the liquid phase of the second portion of the first split stream with the at least partially condensed expanded first portion stream from said boiler/condenser of step (e) and phase separating the combined stream into a vapor phase feed stream and a liquid phase feed stream; (h) introducing the vapor phase feed stream of step (g) into the distillation column for rectification, and (i) removing a gaseous nitrogen stream from the top of the distillation column, condensing a portion of the gaseous nitrogen against oxygen-enriched liquid from the base of the distillation column and condensing another portion of the gaseous nitrogen stream against the liquid phase feed stream of step (g) by indirect heat exchange in a side column to produce a liquid nitrogen product and a gaseous recycle stream to the feed air.

Claim 29

A process for the cryogenic distillative separation of air to produce at least a liquid nitrogen product comprising the steps of: (a) compressing feed air to an elevated pressure and removing water, carbon dioxide and condensibles from the feed air; (b) splitting the feed air into a first split feed stream and a second split feed stream; (c) cooling each split feed stream to a lower temperature by indirect heat exchange against process streams; (d) expanding a first portion of the first split feed stream through a warm expander and recycling a first part of the expanded stream to feed air while providing refrigeration to the feed air by indirect heat exchange; (e) expanding the second split feed stream through a cold expander and introducing a first portion of the expanded stream into a boiler/condenser in the base of a distillation column to provide boil-up in the column and at least partially condense said expanded first portion; (f) cooling and phase separating a second portion of the first split stream and combining the vapor phase of said second portion with said first portion of the expanded stream of step (e) before its introduction into the boiler/condenser; (g) combining the liquid phase of the second portion of the first split stream with the at least partially condensed expanded first portion stream from said boiler/condenser of step (e) and phase separating the combined stream into a vapor phase feed stream and a liquid phase feed stream; (h) introducing the vapor phase feed stream of step (g) into the distillation column for rectification, and (i) removing a gaseous nitrogen stream from the top of the distillation column, condensing a portion of the gaseous nitrogen against oxygen-enriched liquid from the base of the distillation column and condensing another portion of the gaseous nitrogen stream against the liquid phase feed stream of step (g) by indirect heat exchange in a side column to produce a liquid nitrogen product and a gaseous recycle stream to the feed air.