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US5037462A Expired / Lapsed US ⏱️ 0.0 years remaining

Process and device for production of nitrogen

Assignee: Linde GmbH
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Filing: 1987-04-01
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Granted: 1991-08-06
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Expires: 2007-04-01
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Abstract

Abstract In a process for production of nitrogen by low-temperature rectification of air, the air is compressed and divided into two partial streams of which the first partial stream is cooled and fed to a rectification zone, while the second partial stream is further compressed, cooled, expanded and then also fed to the rectification zone. The first partial stream, before it is fed to the rectification zone, is brought into heat exchange relation with the bottom liquid of the rectification zone. A nitrogen product stream is removed from an upper section of the rectification zone.

Inventors

  • 👤 Karl H. Schweigert

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 16:35
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/044; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04296; F25J2200/00; F25J2200/50; F25J2200/72; Y; Y10; Y10S; Y10S62/00; Y10S62/939

Claims Analysis

Total Claims: 22
Claim 1
Independent Claim 183 words
In a process for production of nitrogen by low-temperature rectification of air wherein an air feed stream is compressed and divided into a first partial stream and a second partial stream, said first partial stream is cooled and fed to an elongated vertical rectification zone having an upper part and a lower part, and a nitrogen product stream is discharged from the upper part of said rectification zone, the improvement wherein said second partial stream is separately further compressed, cooled, expanded and also fed to said rectification zone; said first partial stream, before being fed into said rectification zone, is brought into indirect heat exchange with a bottom liquid of said rectification zone; and said bottom liquid is brought into heat exchange with nitrogen gas at the head of said rectification zone whereby bottom liquid evaporates to form a residual gas and said nitrogen gas partially condenses, and at least a portion of said residual gas is used for regeneration of a purification stage for purifying said air feed stream, said purification stage being upstream of the division of said air feed stream.
Claim 2
Dependent Claim 183 words
In a process for production of nitrogen by low-temperature rectification of air wherein an air feed stream is compressed and divided into a first partial stream and a second partial stream, said first partial stream is cooled and fed to an elongated vertical rectification zone having an upper part and a lower part, and a nitrogen product stream is discharged from the upper part of said rectification zone, the improvement wherein said second partial stream is separately further compressed, cooled, expanded and also fed to said rectification zone; said first partial stream, before being fed into said rectification zone, is brought into indirect heat exchange with a bottom liquid of said rectification zone; and said bottom liquid is brought into heat exchange with nitrogen gas at the head of said rectification zone whereby bottom liquid evaporates to form a residual gas and said nitrogen gas partially condenses, and at least a portion of said residual gas is used for regeneration of a purification stage for purifying said air feed stream, said purification stage being upstream of the division of said air feed stream.
Claim 3
Dependent Claim 36 words
A process according to claim 1, wherein expansion of said second partial stream results in production of work and at least a part of the work produced is used for separately compressing said second partial stream.
Claim 4
Dependent Claim 13 words
A process according to claim 2, wherein rectification is performed in one stage.
Claim 5
Dependent Claim 23 words
A process according to claim 2, wherein said nitrogen product stream is discharged from the process at a pressure of about 3-10 bars.
Claim 6
Dependent Claim 23 words
A process according to claim 2, wherein said nitrogen product stream is discharged from the process at a pressure of about 3-6 bars.
Claim 7
Dependent Claim 13 words
A process according to claim 1, wherein rectification is performed in one stage.
Claim 8
Dependent Claim 23 words
A process according to claim 6, wherein said nitrogen product stream is discharged from the process at a pressure of about 3-10 bars.
Claim 9
Dependent Claim 23 words
A process according to claim 6, wherein said nitrogen product stream is discharged from the process at a pressure of about 3-6 bars.
Claim 10
Dependent Claim 23 words
A process according to claim 1, wherein said nitrogen product stream is discharged from the process at a pressure of about 3-10 bars.
Claim 11
Dependent Claim 23 words
A process according to claim 1, wherein said nitrogen product stream is discharged from the process at a pressure of about 3-6 bars.
Claim 12
Dependent Claim 42 words
A process according to claim 1, wherein said second partial stream, immediately prior to its expansion, exhibits a higher temperature than exhibited by said first partial stream immediately before said first partial stream is brought into heat exchange with said bottom liquid.
Claim 13
Dependent Claim 21 words
A process according to claim 1, wherein, after its expansion, said second partial stream is fed directly to said rectification zone.
Claim 14
Dependent Claim 29 words
A process according to claim 1, wherein said heat exchange between said first partial stream and said bottom liquid is conducted within the lower part of said rectification zone.
Claim 15
Dependent Claim 25 words
A process according to claim 1, wherein said bottom liquid, prior to its heat exchange with nitrogen gas, undergoes heat exchange with said residual gas.
Claim 16
Dependent Claim 15 words
The process according to claim 1, wherein said partial stream is expanded in a turbine.
Claim 17
Independent Claim 246 words
An apparatus for production of nitrogen by low-temperature rectification, comprising: a first compressing means for compressing an air feed stream; a single-stage rectification column; a feed conduit in fluid communication with said first compressor and said rectification column; a branch conduit connected to said feed conduit upstream of said rectification column for dividing the air feed stream into a first partial stream, which flows through said feed conduit, and a second partial stream, which flows through said branch conduit; said branch conduit communicating with a second compressing means, a heat exchange means for cooling said second partial stream, expansion means for expanding resultant cooled second partial stream, and said rectification column; said feed conduit communicating with a heat exchange means wherein said first partial stream undergoes heat exchange with separation products from said rectification, and communicating with a second heat exchange means, prior to delivery of said first partial stream to said rectification column, wherein said first partial stream undergoes heat exchange with a bottom liquid from said rectification column; wherein an upper section of said rectification column is provided with an evaporator-condenser for evaporating a bottom liquid from said rectification column to form a residual gas stream and for partially condensing nitrogen gas; and further comprising conduit means communicating with the bottom of said rectification column and heat exchange means wherein bottom liquid from said rectification column undergoes heat exchange with said residual gas stream prior to evaporation of said bottom liquid in said evaporator-condenser.
Claim 18
Independent Claim 246 words
An apparatus for production of nitrogen by low-temperature rectification, comprising: a first compressing means for compressing an air feed stream; a single-stage rectification column; a feed conduit in fluid communication with said first compressor and said rectification column; a branch conduit connected to said feed conduit upstream of said rectification column for dividing the air feed stream into a first partial stream, which flows through said feed conduit, and a second partial stream, which flows through said branch conduit; said branch conduit communicating with a second compressing means, a heat exchange means for cooling said second partial stream, expansion means for expanding resultant cooled second partial stream, and said rectification column; said feed conduit communicating with a heat exchange means wherein said first partial stream undergoes heat exchange with separation products from said rectification, and communicating with a second heat exchange means, prior to delivery of said first partial stream to said rectification column, wherein said first partial stream undergoes heat exchange with a bottom liquid from said rectification column; wherein an upper section of said rectification column is provided with an evaporator-condenser for evaporating a bottom liquid from said rectification column to form a residual gas stream and for partially condensing nitrogen gas; and further comprising conduit means communicating with the bottom of said rectification column and heat exchange means wherein bottom liquid from said rectification column undergoes heat exchange with said residual gas stream prior to evaporation of said bottom liquid in said evaporator-condenser.
Claim 19
Dependent Claim 22 words
An apparatus according to claim 16, wherein said second heat exchange means is positioned in a bottom section of said rectification column.
Claim 20
Dependent Claim 40 words
An apparatus according to claim 16, wherein an upper section of said rectification column is provided with an evaporator-condenser for evaporating a bottom liquid from said rectification column to form a residual gas stream and for partially condensing nitrogen gas.
Claim 21
Dependent Claim 20 words
An apparatus according to claim 16, wherein nitrogen gas is removed from the apparatus without being subjected to further expansion.
Claim 22
Dependent Claim 35 words
An apparatus according to claim 16, wherein said second compressor means is connected to said expansion means whereby work produced by expansion of said second partial stream is used for operating said second compressor means.

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1994-08-05 1995-02-04 1995-08-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-08-05 1999-02-04 1999-08-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-08-05 2003-02-04 2003-08-06 $7700.00 Window Closed / Lapsed

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