Dual feed air pressure nitrogen generator cycle

Claim 2

A process for the production of gaseous nitrogen by the low temperature distillation of air in two distillation columns comprising: (a) producing two different pressure feed air streams by compression in order to have a low pressure feed air stream and a high pressure feed air stream; (b) expanding a process stream through an expansion turbine to reduce its pressure and temperature so as to provide refrigeration for the distillation process wherein the expander flow is uncoupled from mass balance considerations so that only the required process stream flow is taken to the expansion turbine; (c) introducing at least a part of the high pressure feed air stream into a first high pressure, distillation column to provide the required high pressure column feed to generate a low pressure column boilup vapor from a reboiler-condenser; (d) introducing the low pressure feed air stream into a second, low pressure, distillation column; (e) condensing a nitrogen reflux stream in the high pressure column by heat exchange of the nitrogen of the high pressure column against the bottom liquid of the low pressure column in said reboiler-condenser; (f) removing nitrogen-rich liquid from the high pressure column, expanding it and introducing it into the low pressure column as reflux; (g) removing a bottom stream from the high pressure column, expanding it and introducing it into the low pressure column; (h) condensing a nitrogen reflux stream in the low pressure column in a vaporizer-condenser against bottom liquid from said column which is expanded to a lower pressure and temperature and introduced into the vaporizer-condenser, and (i) removing a portion of the nitrogen overhead vapor from the low pressure column as a product.

Claim 3

The process of claim 1 wherein a liquid nitrogen product is removed from the reflux stream of step (e) or step (h).

Claim 4

The process of claim 1 wherein a gaseous waste, oxygen-enriched stream is removed from the overhead of the vaporizer-condenser and is rewarmed against process streams.

Claim 5

The process of claim 3 wherein the expanded process stream of step (b) is the gaseous waste, oxygen-enriched stream.

Claim 6

The process of claim 1 wherein the feed air is initially dried of any moisture and separated from any carbon dioxide by passage through a molecular sieve adsorption system.

Claim 7

The process of claim 1 wherein the two different pressure feed air streams are cooled by heat exchange against process streams.

Claim 8

The process of claim 1 wherein at least a portion of the feed air stream to the low pressure column reboils the low pressure column before being introduced into said column as reflux.

Claim 9

The process of claim 1 wherein the expanded process stream of step (b) is a portion of the high pressure feed air stream.

Claim 10

The process of claim 1 wherein the expanded process stream of step (b) is a nitrogen stream from the overhead of the high pressure, distillation column.

Claim 11

The process of claim 1 wherein the expanded process stream of step (b) is the nitrogen product from the overhead of the low pressure, distillation column.

Claim 12

A process for the production of gaseous nitrogen by the low temperature distillation of air in two distillation columns comprising: (a) producing two different pressure feed air streams by compression in order to have a low pressure feed air stream and a high pressure feed air stream; (b) splitting the high pressure feed air stream into an expander feed air stream and a remaining high pressure feed stream which is introduced into a first, high pressure, distillation column to provide the required high pressure column feed to generate a low pressure column boilup vapor from a reboiler-condenser; (c) expanding the expander feed air stream through an expansion turbine to reduce its pressure and temperature and desuperheating the expanded feed air stream by heat exchange against a process stream wherein the expander flow is uncoupled from mass balance considerations so that only the required feed air stream flow is taken to the expansion turbine; (d) introducing the low pressure feed air stream and the expanded feed air stream into a second, low pressure, distillation column; (e) condensing a nitrogen reflux stream in the high pressure column by heat exchange of the nitrogen of the high pressure column against the bottom liquid of the low pressure column in said reboiler-condenser; (f) removing nitrogen-rich liquid from the high pressure column, expanding it and introducing it into the low pressure column as reflux; (g) removing a bottom stream from the high pressure column, expanding it and introducing it into the low pressure column; (h) condensing a nitrogen reflux stream in the low pressure column in a vaporizer-condenser against bottom liquid from said column which is expanded to a lower pressure and temperature and introduced into the vaporizer-condenser, and (i) removing a portion of the overhead nitrogen vapor from the low pressure column as a product.

Claim 13

A process for the production of gaseous nitrogen by the low temperature distillation of air in two distillation columns comprising: (a) producing two different pressure feed air streams by compression in order to have a low pressure feed air stream and a high pressure feed air stream; (b) splitting the high pressure feed air stream into an expander feed air stream and a remaining high pressure feed stream which is introduced into a first, high pressure, distillation column to provide the required high pressure column feed to generate a low pressure column boilup vapor from a reboiler-condenser; (c) expanding the expander feed air stream through an expansion turbine to reduce its pressure and temperature and desuperheating the expanded feed air stream by heat exchange against a process stream wherein the expander flow is uncoupled from mass balance considerations so that only the required feed air stream flow is taken to the expansion turbine; (d) introducing the low pressure feed air stream and the expanded feed air stream into a second, low pressure, distillation column; (e) condensing a nitrogen reflux stream in the high pressure column by heat exchange of the nitrogen of the high pressure column against the bottom liquid of the low pressure column in said reboiler-condenser; (f) removing nitrogen-rich liquid from the high pressure column, expanding it and introducing it into the low pressure column as reflux; (g) removing a bottom stream from the high pressure column, expanding it and introducing it into the low pressure column; (h) condensing a nitrogen reflux stream in the low pressure column in a vaporizer-condenser against bottom liquid from said column which is expanded to a lower pressure and temperature and introduced into the vaporizer-condenser, and (i) removing a portion of the overhead nitrogen vapor from the low pressure column as a product.

Claim 14

The process of claim 11 wherein a portion of the nitrogen product desuperheats the expanded feed air stream.

Claim 17

The apparatus of claim 13 including means for separating a portion of the high pressure feed air stream for expansion in said turbine and introducing of the turbine exhaust into the low pressure, distillation column.

Claim 18

The apparatus of claim 14 including a desuperheater heat exchanger for cooling the expanded turbine-exhaust against process streams before introducing the turbine exhaust into the low pressure column.

Claim 19

The apparatus of claim 14 including a reboiler in the low pressure column that cools the feed air stream to said column and reboils the fluid in the column.

Claim 20

The apparatus of claim 13 including means for providing reflux to the low pressure column from the vaporizer-condenser.

Claim 21

The apparatus of claim 13 including expansion means for the nitrogen stream of paragraph (e) and the bottom stream of paragraph (f).

Claim 22

The apparatus of claim 13 including a main heat exchanger for cooling the low pressure feed stream and the high pressure feed air stream against process streams.