Elevated pressure air separation cycles with liquid production

Claim 2

In a cryogenic process for the separation of air into at least an oxygen product and a nitrogen product and of which at least a portion of the oxygen product is recovered as a liquid, and wherein the process utilizes a distillation column system having at least two distillation columns, a high pressure distillation column and a low pressure column, which are in thermal communications with each other, wherein the low pressure column operates at a pressure between 9 to 75 psig, wherein the low pressure column produces a low pressure nitrogen product that is at least a portion of the nitrogen product, wherein at least 50% of the feed air to the distillation column system is removed from the low pressure column as said low pressure nitrogen product and wherein said low pressure nitrogen product has a nitrogen concentration of at least 95% and is at a pressure of at least 9 psig, the improvement for producing liquid products in an efficient manner comprising the steps of: (a) partially warming the low pressure nitrogen product by heat exchange against a suitable process stream; (b) isentropically expanding this partially warmed, low pressure nitrogen product in an expander so as a result of this expansion the temperature of the expanded nitrogen is at a lower temperature than the temperature of liquid streams which are removed from the high pressure column; and (c) subcooling the liquid streams removed from the high pressure column by heat exchange against the isentropically expanded nitrogen prior to isenthalpic reduction of the pressures of such liquid streams across a valve.

Claim 3

In a cryogenic process for the separation of air into at least an oxygen product and a nitrogen product and of which at least a portion of the oxygen product is recovered as a liquid, and wherein the process utilizes a distillation column system having at least two distillation columns, a high pressure distillation column and a low pressure column, which are in thermal communication with each other, wherein the low pressure column operates at a pressure between 9 to 75 psig, wherein the low pressure column produces a low pressure nitrogen product that is at least a portion of the nitrogen product, wherein at least 50% of the feed air to the distillation column system is removed from the low pressure column as said low pressure nitrogen product and wherein said low pressure nitrogen product has a nitrogen concentration of at least 95% and is at a pressure of at least 9 psig, the improvement for producing liquid products in an efficient manner comprising the steps of: (a) partially warming the low pressure nitrogen product by heat exchange against a suitable process stream; (b) isentropically expanding this partially warmed, low pressure nitrogen product in an expander so as a result of this expansion the temperature of the expanded nitrogen is at or below the dew point of the feed air to the double column distillation system; and (c) cooling the feed air by heat exchange against the isentropically expanded nitrogen.

Claim 4

In a cryogenic process for the separation of air into at least an oxygen product and a nitrogen product and of which at least a portion of the oxygen product is recovered as a liquid, and wherein the process utilizes a distillation column system having at least two distillation columns, a high pressure distillation column and a low pressure column, which are in thermal communication with each other, wherein the low pressure column operates at a pressure between 9 to 75 psig, wherein the low pressure column produces a low pressure nitrogen product that is at least a portion of the nitrogen product, wherein at least 50% of the feed air to the distillation column system is removed from the low pressure column as said low pressure nitrogen product and wherein said low pressure nitrogen product has a nitrogen concentration of at least 95% and is at a pressure of at least 9 psig, the improvement for producing liquid products in an efficient manner comprising the steps of: (a) partially warming the low pressure nitrogen product by heat exchange against a suitable process stream; (b) isentropically expanding this partially warmed, low pressure nitrogen product in an expander so as a result of this expansion the temperature of the expanded nitrogen is at or below the dew point of the feed air to the double column distillation system; and (c) cooling the feed air by heat exchange against the isentropically expanded nitrogen.

Claim 5

In a cryogenic process for the separation of air into at least an oxygen product and a nitrogen product and of which at least a portion of one of the products produced is recovered as a liquid, and wherein the process utilizes a distillation column system having at least two distillation columns, a high pressure distillation column and a low pressure column, which are in thermal communication with each other, wherein the low pressure column operates at a pressure between 9 to 75 psig, wherein the low pressure column produces a low pressure nitrogen product that is at least part of the nitrogen product, wherein at least 50% of the feed air to the distillation column system is removed from the low pressure column as said low pressure nitrogen product and wherein said low pressure nitrogen product has a nitrogen concentration of at least 95% and is at a pressure of at least 9 psig, the improvement for producing liquid products in an efficient manner comprising the steps of: (a) partially warming the low pressure nitrogen product stream by heat exchange against a suitable process stream; (b) dividing the partially warmed, low pressure nitrogen product into two substreams, a first substream and a second substream; (c) isentropically expanding the first substream in an expander so as a result of this expansion the temperature of the expanded first substream is at a lower temperature than the temperature of liquid streams which are removed from the high pressure column; (d) subcooling the liquid streams removed from the high pressure column by heat exchange against the isentropically expanded first substream prior to isenthalpic reduction of the pressures of such liquid streams across a valve; (e) warming the second substream by heat exchange against a suitable process stream; (f) isentropically expanding this partially warmed, second substream product in an expander so as a result of this expansion the temperature of the expanded second substream is at or below the dew point of the feed air to the double column distillation system; and (g) cooling the feed air by heat exchange against the isentropically expanded first and second substreams.

Claim 6

In a cryogenic process for the separation of air into at least an oxygen product and a nitrogen product and of which at least a portion of one of the products produced is recovered as a liquid, and wherein the process utilizes a distillation column system having at least two distillation columns, a high pressure distillation column and a low pressure column, which are in thermal communication with each other, wherein the low pressure column operates at a pressure between 9 to 75 psig, wherein the low pressure column produces a low pressure nitrogen product that is at least part of the nitrogen product, wherein at least 50% of the feed air to the distillation column system is removed from the low pressure column as said low pressure nitrogen product and wherein said low pressure nitrogen product has a nitrogen concentration of at least 95% and is at a pressure of at least 9 psig, the improvement for producing liquid products in an efficient manner comprising the steps of: (a) partially warming the low pressure nitrogen product stream by heat exchange against a suitable process stream; (b) dividing the partially warmed, low pressure nitrogen product into two substreams, a first substream and a second substream; (c) isentropically expanding the first substream in an expander so as a result of this expansion the temperature of the expanded first substream is at a lower temperature than the temperature of liquid streams which are removed from the high pressure column; (d) subcooling the liquid streams removed from the high pressure column by heat exchange against the isentropically expanded first substream prior to isenthalpic reduction of the pressures of such liquid streams across a valve; (e) warming the second substream by heat exchange against a suitable process stream; (f) isentropically expanding this partially warmed, second substream product in an expander so as a result of this expansion the temperature of the expanded second substream is at or below the dew point of the feed air to the double column distillation system; and (g) cooling the feed air by heat exchange against the isentropically expanded first and second substreams.

Claim 7

The process of claim 2 wherein the cooling of the feed air by heat exchange with the isentropically expanded nitrogen product of step (c) also partially condenses the feed air stream.

Claim 8

The process of claim 3 wherein the cooling of the feed air by heat exchange with the isentropically expanded second substream of step (g) also partially condenses the feed air stream.

Claim 9

The process of claim 3 which further comprises compressing and aftercooling the second substream prior to the isentropic expansion.

Claim 10

The process of claim 3 wherein at least a portion of the warmed isentropically expanded second substream of step (g) is used to regenerate mole sieve beds used to preclean the feed air stream.

Claim 11

The process of claim 3 wherein at least a portion of the isentropically expanded first substream of step (d) is used to regenerate mole sieve beds used to pre-clean the feed air stream.

Claim 12

The process of claim 1 wherein a portion of the warmed nitrogen of step (a) is isentropically expanded in a separate expander to a pressure which is between 1 to 3 psi lower than the discharge pressure of the isentropically expanded nitrogen of step (b) and wherein said isentropically expanded portion is used to regenerate mole sieve beds used to pre-clean the feed air stream.

Claim 13

The process of claim 2 wherein a portion of the warmed nitrogen of step (a) is isentropically expanded in a separate expander to a pressure which is between 1 to 3 psi lower than the discharge pressure of the isentropically expanded nitrogen of step (b) and wherein said isentropically expanded portion is used to regenerate mole sieve beds used to pre-clean the feed air stream.