US5245832A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Triple column cryogenic rectification system
Assignee: Praxair Technology Inc
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Filing: 1992-04-20
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Granted: 1993-09-21
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Expires: 2012-04-20
Abstract
Abstract A direct sequenced three column cryogenic rectification system wherein material flow is unidirectional from higher to lower pressure through the system enabling high recovery of each of the three major components of feed air.
Inventors
- 👤 Mark J. Roberts
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 03:56
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04642; F25J3/04648; F25J3/04654; F25J3/04709; F25J3/04715; F25J3/04006; F25J3/04078; F25J3/0409; F25J3/04151; F25J3/04187; F25J3/04193; F25J3/04206; F25J3/04212; F25J3/04248; F25J3/04284; F25J3/04309; F25J3/04333; F25J3/04351; F25J2200/00; F25J2200/08; F25J2200/50; F25J2200/54; F25J2205/00; F25J2205/02; F25J2245/00; F25J2245/42; F25J2245/50; F25J2250/00; F25J2250/30; F25J2250/42; F25J2250/50; F25J2250/58; Y; Y10; Y10S; Y10S62/00; Y10S62/90; Y10S62/923; Y10S62/924
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
264 words
A method for producing nitrogen, oxygen and argon product by the cryogenic rectification of air comprising: (A) introducing feed air into a first column operating at a pressure within the range of from 150 to 350 psia and separating the feed air by cryogenic rectification within the first column into nitrogen-enriched vapor and oxygen-argon-enriched fluid; (B) passing oxygen-argon-enriched fluid from the first column into a second column operating at a pressure less than that of the first column and having a bottom reboiler, and separating oxygen-argon-enriched fluid by cryogenic rectification within the second column into nitrogen-rich vapor and oxygen-argon-rich fluid; (C) condensing nitrogen-enriched vapor by indirect heat exchange with oxygen-argon-rich fluid in the second column bottom reboiler to produce nitrogen-enriched liquid and oxygen-argon-rich vapor, employing nitrogen-enriched liquid as reflux liquid for the first column, and employing oxygen-argon-rich vapor as reflux vapor for the second column; (D) passing oxygen-argon-rich fluid from the second column into a third column operating at a pressure less than that of the second column and having a bottom reboiler, and separating oxygen-argon-rich fluid by cryogenic rectification within the third column into argon-rich fluid and oxygen-rich fluid; (E) recovering a first portion of nitrogen-rich vapor as product nitrogen; (F) condensing a second portion of nitrogen-rich vapor by indirect heat exchange with oxygen-rich fluid in the third column bottom reboiler to produce nitrogen-rich liquid and oxygen-rich vapor, employing nitrogen-rich liquid as reflux liquid for the second column, and employing oxygen-rich vapor as reflux vapor for the third column; and (G) recovering oxygen-rich fluid as product oxygen and argon-rich fluid as product argon.
Claim 2
Independent Claim
264 words
A method for producing nitrogen, oxygen and argon product by the cryogenic rectification of air comprising: (A) introducing feed air into a first column operating at a pressure within the range of from 150 to 350 psia and separating the feed air by cryogenic rectification within the first column into nitrogen-enriched vapor and oxygen-argon-enriched fluid; (B) passing oxygen-argon-enriched fluid from the first column into a second column operating at a pressure less than that of the first column and having a bottom reboiler, and separating oxygen-argon-enriched fluid by cryogenic rectification within the second column into nitrogen-rich vapor and oxygen-argon-rich fluid; (C) condensing nitrogen-enriched vapor by indirect heat exchange with oxygen-argon-rich fluid in the second column bottom reboiler to produce nitrogen-enriched liquid and oxygen-argon-rich vapor, employing nitrogen-enriched liquid as reflux liquid for the first column, and employing oxygen-argon-rich vapor as reflux vapor for the second column; (D) passing oxygen-argon-rich fluid from the second column into a third column operating at a pressure less than that of the second column and having a bottom reboiler, and separating oxygen-argon-rich fluid by cryogenic rectification within the third column into argon-rich fluid and oxygen-rich fluid; (E) recovering a first portion of nitrogen-rich vapor as product nitrogen; (F) condensing a second portion of nitrogen-rich vapor by indirect heat exchange with oxygen-rich fluid in the third column bottom reboiler to produce nitrogen-rich liquid and oxygen-rich vapor, employing nitrogen-rich liquid as reflux liquid for the second column, and employing oxygen-rich vapor as reflux vapor for the third column; and (G) recovering oxygen-rich fluid as product oxygen and argon-rich fluid as product argon.
Claim 3
Dependent Claim
26 words
The method of claim 1 wherein the oxygen-rich fluid is increased in pressure and vaporized by indirect heat exchange with condensing nitrogen-enriched vapor prior to recovery.
Claim 4
Dependent Claim
13 words
The method of claim 1 wherein nitrogen-rich vapor is condensed prior to recovery.
Claim 5
Dependent Claim
15 words
The method of claim 1 additionally comprising recovering nitrogen-containing fluid taken from the first column.
Claim 6
Dependent Claim
15 words
The method of claim 1 additionally comprising recovering oxygen-containing fluid taken from the second column.
Claim 7
Dependent Claim
160 words
Apparatus for producing nitrogen, oxygen and argon product by cryogenic rectification comprising: (A) a first column having feed introduction means; (B) a second column having a bottom reboiler, means for passing fluid from the lower portion of the first column into the second column, and means for passing fluid from the upper portion of the first column into the second column bottom reboiler and from the second column bottom reboiler into the first column; (C) means for recovering product from the second column; (D) a third column having a bottom reboiler, means for passing fluid from the second column into the third column, and means for passing fluid from the upper portion of the second column into the third column bottom reboiler and from the third column bottom reboiler into the second column; (E) means for recovering product from the lower portion of the third column; and (F) means for recovering product from the upper portion of the third column.
Claim 8
Dependent Claim
160 words
Apparatus for producing nitrogen, oxygen and argon product by cryogenic rectification comprising: (A) a first column having feed introduction means; (B) a second column having a bottom reboiler, means for passing fluid from the lower portion of the first column into the second column, and means for passing fluid from the upper portion of the first column into the second column bottom reboiler and from the second column bottom reboiler into the first column; (C) means for recovering product from the second column; (D) a third column having a bottom reboiler, means for passing fluid from the second column into the third column, and means for passing fluid from the upper portion of the second column into the third column bottom reboiler and from the third column bottom reboiler into the second column; (E) means for recovering product from the lower portion of the third column; and (F) means for recovering product from the upper portion of the third column.
Claim 9
Dependent Claim
26 words
The apparatus of claim 6 wherein the means for recovering product from the lower portion of the third column includes a pump and a product boiler.
Claim 10
Dependent Claim
19 words
The apparatus of claim 6 further comprising means for recovering product from the upper portion of the first column.
Claim 11
Dependent Claim
54 words
The apparatus of claim 6 further comprising means for recovering additional product from the second column wherein said means for recovering additional product communicates with the second column at a point below the point from which the means for passing fluid from the second column into the third column communicates with the second 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) | 1996-09-20 | 1997-03-22 | 1997-09-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-09-20 | 2001-03-22 | 2001-09-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-09-20 | 2005-03-22 | 2005-09-21 | $7700.00 | Window Closed / Lapsed |