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US5098457A
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Method and apparatus for producing elevated pressure nitrogen
Assignee: Praxair Technology Inc
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Filing: 1991-01-22
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Granted: 1992-03-24
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Expires: 2011-01-22
Abstract
Abstract A method and apparatus for producing elevated pressure nitrogen with improved recovery comprising a primary column and a lower pressure auxiliary column wherein auxiliary column top vapor is condensed, pressurized and passed into the primary column.
Inventors
- 👤 Harry Cheung
- 👤 Dante P. Bonaquist
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 19:48
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04303; F25J3/04151; F25J3/04187; F25J3/04193; F25J3/0423; F25J3/04236; F25J3/04406; F25J3/04424; F25J2200/00; F25J2200/20; F25J2200/50; F25J2200/54; F25J2235/00; F25J2235/42; F25J2245/00; F25J2245/42; Y; Y10; Y10S; Y10S62/00; Y10S62/939
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
142 words
A method for producing elevated pressure nitrogen with improved recovery comprising: (A) providing compressed feed air into a primary column operating at a pressure within the range of from 80 to 150 pounds per square inch absolute; (B) separating the feed air in the primary column into nitrogen-richer component and oxygen-enriched component; (C) providing oxygen-enriched component into an auxiliary column operating at a pressure less than that of the primary column; (D) separating oxygen-enriched component into nitrogen-enriched vapor and oxygen-richer liquid; (E) condensing nitrogen-enriched vapor by indirect heat exchange with oxygen-richer liquid to produce nitrogen-enriched liquid; (F) increasing the pressure of the nitrogen-enriched liquid to substantially the operating pressure of the primary column; (G) providing pressurized nitrogen-enriched liquid into the primary column for further production of nitrogen-richer component; and (H) recovering nitrogen-richer component from the primary column as product elevated pressure nitrogen.
Claim 2
Independent Claim
142 words
A method for producing elevated pressure nitrogen with improved recovery comprising: (A) providing compressed feed air into a primary column operating at a pressure within the range of from 80 to 150 pounds per square inch absolute; (B) separating the feed air in the primary column into nitrogen-richer component and oxygen-enriched component; (C) providing oxygen-enriched component into an auxiliary column operating at a pressure less than that of the primary column; (D) separating oxygen-enriched component into nitrogen-enriched vapor and oxygen-richer liquid; (E) condensing nitrogen-enriched vapor by indirect heat exchange with oxygen-richer liquid to produce nitrogen-enriched liquid; (F) increasing the pressure of the nitrogen-enriched liquid to substantially the operating pressure of the primary column; (G) providing pressurized nitrogen-enriched liquid into the primary column for further production of nitrogen-richer component; and (H) recovering nitrogen-richer component from the primary column as product elevated pressure nitrogen.
Claim 3
Dependent Claim
22 words
The method of claim 1 wherein a portion of the nitrogen-richer component is condensed and employed in the primary column as reflux.
Claim 4
Dependent Claim
28 words
The method of claim 2 wherein the nitrogen-richer component is condensed by indirect heat exchange with oxygen-enriched component and resulting oxygen-enriched component is passed into the auxiliary column.
Claim 5
Dependent Claim
36 words
The method of claim 3 wherein the oxygen-enriched component is partially vaporized by the indirect heat exchange with condensing nitrogen-richer component and both the resulting oxygen-enriched vapor and oxygen-enriched liquid are passed into the auxiliary column.
Claim 6
Dependent Claim
17 words
The method of claim 1 wherein the pressure of the nitrogen-enriched liquid is increased by liquid pumping.
Claim 7
Dependent Claim
26 words
The method of claim 1 further comprising liquefying a portion of the compressed feed air prior to the introduction of such portion into the primary column.
Claim 8
Dependent Claim
31 words
The method of claim 6 wherein the said feed air portion is liquified by indirect heat exchange with bottoms of the auxiliary column thereby providing vapor upflow for the auxiliary column.
Claim 9
Dependent Claim
35 words
The method of claim 1 further comprising turboexpanding a portion of the compressed feed air to generate refrigeration and introducing the turboexpanded feed air portion into the auxiliary column to provide refrigeration into the system.
Claim 10
Dependent Claim
33 words
The method of claim 1 further comprising turboexpanding a portion of the oxygen-enriched component and passing said turboexpanded portion in indirect heat exchange with compressed feed air to provide refrigeration into the system.
Claim 11
Dependent Claim
38 words
The method of claim 1 wherein a portion of the nitrogen-richer component is turboexpanded to generate refrigeration and the turboexpanded nitrogen-richer portion is passed in indirect heat exchange with compressed feed air to provide refrigeration into the system.
Claim 12
Dependent Claim
101 words
Apparatus for producing elevated pressure nitrogen with improved recovery comprising: (A) a primary column having a top condenser and means for providing feed into the primary column; (B) means for providing fluid from the lower portion of the primary column into the top condenser; (C) an auxiliary column having a top condenser; (D) means for providing fluid from the primary column top condenser into the auxiliary column; (E) means for providing liquid from the auxiliary column top condenser into the primary column including means for increasing the pressure of said liquid; and (F) means for recovering product from the primary column.
Claim 13
Dependent Claim
101 words
Apparatus for producing elevated pressure nitrogen with improved recovery comprising: (A) a primary column having a top condenser and means for providing feed into the primary column; (B) means for providing fluid from the lower portion of the primary column into the top condenser; (C) an auxiliary column having a top condenser; (D) means for providing fluid from the primary column top condenser into the auxiliary column; (E) means for providing liquid from the auxiliary column top condenser into the primary column including means for increasing the pressure of said liquid; and (F) means for recovering product from the primary column.
Claim 14
Dependent Claim
14 words
The apparatus of claim 11 wherein the pressure increasing means comprises a liquid pump.
Claim 15
Dependent Claim
28 words
The apparatus of claim 11 further comprising a turboexpander, means to provide feed into the turboexpander and means to provide feed from the turboexpander into the auxiliary column.
Claim 16
Dependent Claim
36 words
The apparatus of claim 11 further comprising a turboexpander, means to provide fluid from the primary column top condenser into the turboexpander and means to provide fluid from the turboexpander in indirect heat exchange with feed.
Claim 17
Dependent Claim
25 words
The apparatus of claim 11 further comprising means to liquefy a portion of the feed prior to that portion being provided into the primary column.
Claim 18
Dependent Claim
26 words
The apparatus of claim 15 wherein the means for liquefying said portion of the feed comprises a reboiler in the lower portion of the auxiliary column.
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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) | 1995-03-24 | 1995-09-23 | 1996-03-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-03-24 | 1999-09-23 | 2000-03-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-03-24 | 2003-09-23 | 2004-03-24 | $7700.00 | Window Closed / Lapsed |