Process and apparatus for producing nitrogen from air

Claim 1

A process for the recovery of substantially pure nitrogen product at superatmospheric pressure from air comprising the steps of: (a) compressing a gaseous feed air; (b) cooling the compressed air in a heat exchanger against enriched oxygen and nitrogen product streams; (c) introducing the cooled and compressed air to an intermediate stage of a single distillation column; (d) separating a substantially pure gaseous nitrogen overhead and an oxygen enriched liquid bottoms from the column; (e) forwarding substantially all of the oxygen enriched liquid bottoms and a first portion of the gaseous nitrogen overhead to a condenser and therein indirectly exchanging heat between the bottoms and overhead thereby boiling up an oxygen enriched gas stream and condensing a liquid nitrogen stream; (f) recycling a first major portion of the liquid nitrogen stream to the top of the distillation column as a reflux; (g) compressing at least a first portion of the oxygen enriched gas stream at about the temperature of the distillation column and recycling the compressed oxygen enriched gas stream to the bottom of the distillation column thereby enhancing nitrogen product recovery from the air; (h) expanding a second portion of the oxygen enriched gas stream exiting the condenser in an expanding means thereby generating work output to both provide refrigeration for the process and to compress the first portion of the oxygen enriched gas stream which is recycled to the bottom of the distillation column; (i) warming the second remaining portion of the gaseous nitrogen overhead in the heat exchanger against the compressed air; and (j) recovering the warmed nitrogen overhead as a substantially pure nitrogen product from the heat exchanger.

Claim 11

An apparatus for the production of nitrogen product from air comprising: (a) a first compressor for increasing the pressure of a gaseous feed air; (b) a heat exchanger for cooling the high pressure air with products of the distilled feed air; (c) a distillation column for separating the cooled air into a substantially pure gaseous nitrogen overhead and an oxygen enriched liquid bottom; (d) a condenser for at least partially condensing the gaseous nitrogen overhead to form a liquid nitrogen stream via indirect heat exchange with oxygen enriched liquid bottoms to form an oxygen enriched gas stream; (e) a first recycle means for returning a first major portion of the cold liquid nitrogen stream from the condenser to the distillation column as a reflux; (f) a second compressor for increasing the pressure of a first portion of the oxygen enriched gas stream at about the temperature of the distillation column from the condenser; (g) a second recycle means for returning the high pressure oxygen enriched gas stream to the bottom of the distillation column thereby enhancing nitrogen product recovery; (h) an expansion means for expanding a second portion of the oxygen enriched gas stream from the condenser thereby generating work to provide refrigeration for the process and to power the second compressor; wherein the nitrogen product is recovered from the first heat exchanger.

Claim 12

An apparatus for the production of nitrogen product from air comprising: (a) a first compressor for increasing the pressure of a gaseous feed air; (b) a heat exchanger for cooling the high pressure air with products of the distilled feed air; (c) a distillation column for separating the cooled air into a substantially pure gaseous nitrogen overhead and an oxygen enriched liquid bottom; (d) a condenser for at least partially condensing the gaseous nitrogen overhead to form a liquid nitrogen stream via indirect heat exchange with oxygen enriched liquid bottoms to form an oxygen enriched gas stream; (e) a first recycle means for returning a first major portion of the cold liquid nitrogen stream from the condenser to the distillation column as a reflux; (f) a second compressor for increasing the pressure of a first portion of the oxygen enriched gas stream at about the temperature of the distillation column from the condenser; (g) a second recycle means for returning the high pressure oxygen enriched gas stream to the bottom of the distillation column thereby enhancing nitrogen product recovery; (h) an expansion means for expanding a second portion of the oxygen enriched gas stream from the condenser thereby generating work to provide refrigeration for the process and to power the second compressor; wherein the nitrogen product is recovered from the first heat exchanger.