Process and installation for the production of oxygen gas under high pressure by air distillation

Claim 2

A process for the production of high-pressure oxygen gas by distilling air in an air distillation column, wherein nitrogen withdrawn from the column is compressed and heated to an oxygen heating pressure by a cycle compressor, said process comprising the steps of withdrawing oxygen in liquid form from the distillation apparatus, pumping the withdrawn oxygen to a high production pressure, and heating the oxygen at said high production pressure in a single heat transfer stage by heat exchange only with said nitrogen compressed to said oxygen heating pressure by said cycle compressor.

Claim 3

A process according to claim 1, wherein part of the nitrogen withdrawn from the column is compressed by said cycle compressor to a high cycle pressure, and part of the nitrogen withdrawn from the column is compressed to a high oxygen heating pressure that is different from said high cycle pressure.

Claim 4

A process according to claim 1 wherein said cycle compressor supplies process nitrogen at another pressure no higher than said high oxygen heating pressure.

Claim 5

A process for the production of high-pressure oxygen gas by distilling air in an air distillation column which includes a double distillation column comprising a medium-pressure column and a low-pressure column; wherein nitrogen withdrawn from the column is compressed by a cycle compressor, said process comprising the steps of withdrawing oxygen in liquid form from the distillation apparatus, pumping the withdrawn oxygen to a high production pressure, heating the oxygen at said high production pressure by heat exchange only with said nitrogen compressed to an oxygen heating pressure by said cycle compressor, withdrawing nitrogen gas from said medium pressure column, cooling the nitrogen that has been heat-exchanged with said high production pressure oxygen by further heat exchange with said nitrogen gas withdrawn from the medium-pressure column, reducing said cooled nitrogen to said medium pressure to produce two-phase nitrogen, and feeding liquid nitrogen to said medium-pressure column.

Claim 6

A process for the production of high-pressure oxygen gas by distilling air in an air distillation column which includes a double distillation column comprising a medium-pressure column and a low-pressure column; wherein nitrogen withdrawn from the column is compressed by a cycle compressor, said process comprising the steps of withdrawing oxygen in liquid form from the distillation apparatus, pumping the withdrawn oxygen to a high production pressure, heating the oxygen at said high production pressure by heat exchange only with said nitrogen compressed to an oxygen heating pressure by said cycle compressor, withdrawing nitrogen gas from said medium pressure column, cooling the nitrogen that has been heat-exchanged with said high production pressure oxygen by further heat exchange with said nitrogen gas withdrawn from the medium-pressure column, reducing said cooled nitrogen to said medium pressure to produce two-phase nitrogen, and feeding liquid nitrogen to said medium-pressure column.

Claim 7

A process according to claim 4, further comprising the step of reducing to an intermediate pressure, that is greater than said medium pressure, the pressure of the nitrogen gas that has cooled by heat exchange with said high production pressure oxygen before the cooled nitrogen gas is heat exchanged with said withdrawn nitrogen gas.

Claim 8

An installation for the production of high-pressure oxygen gas by air distillation having an air distillation column, a first heat exchanger incapable of withstanding a given high pressure and having a cycle compressor for compressing nitrogen withdrawn from the distillation column to an oxygen heating pressure at least equal to said given high pressure, said installation including a pump for bringing liquid oxygen withdrawn from the distillation column to a high pressure at least equal to said given high pressure, a second heat exchanger capable of withstanding said given high pressure for heat-exchanging said liquid oxygen at said high pressure with said nitrogen compressed by the cycle compressor to said oxygen heating pressure and means for coupling said liquid oxygen at said high pressure from said pump to said second heat exchanger only.

Claim 9

An installation for the production of high-pressure oxygen gas by air distillation having an air distillation column, a first heat exchanger incapable of withstanding a given high pressure and having a cycle compressor for compressing nitrogen withdrawn from the distillation column to an oxygen heating pressure at least equal to said given high pressure, said installation including a pump for bringing liquid oxygen withdrawn from the distillation column to a high pressure at least equal to said given high pressure, a second heat exchanger capable of withstanding said given high pressure for heat-exchanging said liquid oxygen at said high pressure with said nitrogen compressed by the cycle compressor to said oxygen heating pressure and means for coupling said liquid oxygen at said high pressure from said pump to said second heat exchanger only.

Claim 10

The installation according to claim 6 wherein the cycle compressor has a separate stage for compressing nitrogen to said oxygen heating pressure that is different from the high pressure of the refrigeration cycle.

Claim 11

The installation according to claim 7 wherein the cycle compressor includes an outlet connected to a pipe to supply nitrogen at a high pressure that does not exceed said oxygen heating pressure.

Claim 12

An installation for the production of high-pressure oxygen gas by air distillation having an air distillation column which is a double distillation column type having a medium-pressure column and a low-pressure column; a first heat exchange means incapable of withstanding a given high pressure and having a cycle compressor for compressing nitrogen withdrawn from the distillation column to an oxygen heating pressure at least equal to said given high pressure, said installation including a pump for bringing liquid oxygen withdrawn from the distillation column to a high pressure at least equal to said given high pressure, a second heat exchange means capable of withstanding said given high pressure for heat-exchanging said liquid oxygen at said high pressure with said nitrogen compressed by the cycle compressor to said oxygen heating pressure, and a third heat exchange means which is a countercurrent-loop heat exchanger having first passages for heating medium-pressure nitrogen gas, said first passages being in heat-exchange relationship with second passages for cooling nitrogen at a high cycle pressure and with third passages for cooling nitrogen at an intermediate pressure, said third passages being an extension of said second passages and having an intake coupled to an outlet of nitrogen passages included in said second heat exchange means, said third passages having an outlet coupled to the medium-pressure column via a pressure-reduction valve.

Claim 13

An installation for the production of high-pressure oxygen gas by air distillation having an air distillation column which is a double distillation column type having a medium-pressure column and a low-pressure column; a first heat exchange means incapable of withstanding a given high pressure and having a cycle compressor for compressing nitrogen withdrawn from the distillation column to an oxygen heating pressure at least equal to said given high pressure, said installation including a pump for bringing liquid oxygen withdrawn from the distillation column to a high pressure at least equal to said given high pressure, a second heat exchange means capable of withstanding said given high pressure for heat-exchanging said liquid oxygen at said high pressure with said nitrogen compressed by the cycle compressor to said oxygen heating pressure, and a third heat exchange means which is a countercurrent-loop heat exchanger having first passages for heating medium-pressure nitrogen gas, said first passages being in heat-exchange relationship with second passages for cooling nitrogen at a high cycle pressure and with third passages for cooling nitrogen at an intermediate pressure, said third passages being an extension of said second passages and having an intake coupled to an outlet of nitrogen passages included in said second heat exchange means, said third passages having an outlet coupled to the medium-pressure column via a pressure-reduction valve.

Claim 14

The installation according to claim 9 further comprising a pressure reduction valve for coupling said intake of said third passages to said outlet of nitrogen passages included in said third heat exchange means.

Claim 15

The installation according to claim 9 wherein said third heat exchange means is separate from said first and second heat exchange means.