US5233838A
Expired / Lapsed
US
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Auxiliary column cryogenic rectification system
Assignee: Praxair Technology Inc
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Filing: 1992-06-01
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Granted: 1993-08-10
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Expires: 2012-06-01
Abstract
Abstract A cryogenic rectification system having an auxiliary column and a double column plant wherein liquid oxygen from the double column plant is vaporized prior to recovery against auxiliary column top vapor producing additional reflux for the double column plant thereby sustaining oxygen recovery under elevated pressure conditions.
Inventors
- 👤 Henry E. Howard
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:20
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04187; F25J3/04193; F25J3/04206; F25J3/04212; F25J3/042; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04303; F25J3/04436; F25J3/04448; F25J2200/00; F25J2200/20; F25J2250/00; F25J2250/30; F25J2250/50; Y; Y10; Y10S; Y10S62/00; Y10S62/939
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
173 words
A method for the cryogenic rectification of feed air comprising: (A) providing feed air into a double column air separation plant having a higher pressure column and a lower Pressure column and separating the feed air by cryogenic rectification in the double column plant into nitrogen vapor and oxygen liquid; (B) providing secondary feed air into an auxiliary column operating at a pressure less than that of said higher pressure column and separating the secondary feed air by cryogenic rectification in the auxiliary column into nitrogen-enriched vapor and oxygen-enriched liquid; (C) passing oxygen-enriched liquid from the auxiliary column into the double column air separation plant, withdrawing oxygen liquid from the double column air separation plant, and reducing the pressure of the withdrawn oxygen liquid; (D) condensing nitrogen-enriched vapor by indirect heat exchange with reduced pressure oxygen liquid and passing at least a portion of the resulting condensed nitrogen-enriched fluid into the double column air separation plant; and (E) recovering oxygen fluid resulting from the indirect heat exchange with nitrogen-enriched vapor as product oxygen.
Claim 2
Independent Claim
173 words
A method for the cryogenic rectification of feed air comprising: (A) providing feed air into a double column air separation plant having a higher pressure column and a lower Pressure column and separating the feed air by cryogenic rectification in the double column plant into nitrogen vapor and oxygen liquid; (B) providing secondary feed air into an auxiliary column operating at a pressure less than that of said higher pressure column and separating the secondary feed air by cryogenic rectification in the auxiliary column into nitrogen-enriched vapor and oxygen-enriched liquid; (C) passing oxygen-enriched liquid from the auxiliary column into the double column air separation plant, withdrawing oxygen liquid from the double column air separation plant, and reducing the pressure of the withdrawn oxygen liquid; (D) condensing nitrogen-enriched vapor by indirect heat exchange with reduced pressure oxygen liquid and passing at least a portion of the resulting condensed nitrogen-enriched fluid into the double column air separation plant; and (E) recovering oxygen fluid resulting from the indirect heat exchange with nitrogen-enriched vapor as product oxygen.
Claim 3
Dependent Claim
27 words
The method of claim 1 wherein the oxygen-enriched liquid from the auxiliary column is passed into the lower pressure column of the double column air separation plant.
Claim 4
Dependent Claim
28 words
The method of claim 1 wherein the said portion of the condensed nitrogen-enriched fluid is passed into the lower pressure column of the double column air separation plant.
Claim 5
Dependent Claim
13 words
The method of claim 1 further comprising recovering nitrogen vapor as product nitrogen.
Claim 6
Dependent Claim
14 words
The method of claim 1 further comprising recovering some nitrogen-enriched vapor as product nitrogen.
Claim 7
Dependent Claim
15 words
The method of claim 1 further comprising recovering some oxygen liquid as liquid oxygen product.
Claim 8
Dependent Claim
16 words
The method of claim 1 further comprising recovering some condensed nitrogen fluid as liquid nitrogen product.
Claim 9
Dependent Claim
20 words
The method of claim 1 wherein the secondary feed air is expanded prior to being provided into the auxiliary column.
Claim 10
Dependent Claim
145 words
Apparatus for the cryogenic rectification of feed air comprising: (A) a double column air separation plant having a higher pressure column and a lower pressure column, and means for providing feed air into the double column air separation plant; (B) an auxiliary column having a top condenser and means for providing feed air into the auxiliary column; (C) means for passing fluid from the lower portion of the auxiliary column into the double column air separation plant, and means for passing fluid from the upper portion of the auxiliary column into the top condenser; (D) means for passing fluid from the double column air separation plant to pressure reducing means and from the pressure reducing means into the top condenser; (E) means for passing fluid from the top condenser into the double column air separation plant and means for recovering fluid from the top condenser.
Claim 11
Dependent Claim
145 words
Apparatus for the cryogenic rectification of feed air comprising: (A) a double column air separation plant having a higher pressure column and a lower pressure column, and means for providing feed air into the double column air separation plant; (B) an auxiliary column having a top condenser and means for providing feed air into the auxiliary column; (C) means for passing fluid from the lower portion of the auxiliary column into the double column air separation plant, and means for passing fluid from the upper portion of the auxiliary column into the top condenser; (D) means for passing fluid from the double column air separation plant to pressure reducing means and from the pressure reducing means into the top condenser; (E) means for passing fluid from the top condenser into the double column air separation plant and means for recovering fluid from the top condenser.
Claim 12
Dependent Claim
32 words
The apparatus of claim 9 wherein the means for passing fluid from the lower portion of the auxiliary column into the double column air separation plant communicates with the lower pressure column.
Claim 13
Dependent Claim
28 words
The apparatus of claim 9 wherein the means for passing fluid from the top condenser into the double column air separation plant communicates with the lower pressure column.
Claim 14
Dependent Claim
21 words
The apparatus of claim 9 further comprising means for recovering fluid withdrawn from the upper portion of the lower pressure column.
Claim 15
Dependent Claim
19 words
The apparatus of claim 9 wherein the means for providing feed air into the auxiliary column comprises an expander.
Claim 16
Dependent Claim
19 words
The apparatus of claim 9 further comprising means for passing fluid from the top condenser into 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) | 1996-08-09 | 1997-02-08 | 1997-08-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-08-09 | 2001-02-08 | 2001-08-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-08-09 | 2005-02-08 | 2005-08-10 | $7700.00 | Window Closed / Lapsed |