Patent FR1557726A successfully refreshed from Google Patents.
Patent US5440884A successfully refreshed from Google Patents.
US5440884A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Cryogenic air separation system with liquid air stripping
Assignee: Praxair Technology Inc
•
Filing: 1994-07-14
•
Granted: 1995-08-15
•
Expires: 2014-07-14
Abstract
Abstract A cryogenic rectification system which advantageously separates feed air wherein the thermodynamic irreversibility of the argon column top condenser and the lower pressure column is reduced by using a stripping column upstream of the double column main plant.
Inventors
- 👤 Dante P. Bonaquist
- 👤 Michael J. Lockett
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 12:14
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04187; F25J3/04193; F25J3/04206; F25J3/04006; F25J3/04078; F25J3/0409; F25J3/04103; F25J3/04163; F25J3/04169; F25J3/04175; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04296; F25J3/04303; F25J3/04406; F25J3/04412; F25J3/04642; F25J3/04648; F25J3/04654; F25J3/04666; F25J3/04672; F25J3/04678; F25J3/04703; F25J3/04763; F25J3/04866; F25J3/04872; F25J2200/00; F25J2200/38; F25J2200/90; F25J2235/00; F25J2235/58; F25J2250/00; F25J2250/30; F25J2250/40; F25J2250/50; Y; Y10; Y10S; Y10S62/00; Y10S62/923; Y10S62/924
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
159 words
A method for the cryogenic rectification of feed air employing a double column main plant, comprising a higher pressure column and a lower pressure column, and an argon column having a top condenser, comprising: (A) condensing a portion of the feed air to produce liquid feed air; (B) passing liquid feed air and gaseous feed air into a stripping column and passing liquid feed air against gaseous feed air in the stripping column to produce stripping column product gas, having a nitrogen concentration which exceeds that of air, and stripping column product liquid, having an oxygen concentration which exceeds 25 mole percent; (C) passing stripping column product gas into the higher pressure column for separation by cryogenic rectification; (D) at least partially vaporizing stripping column product liquid by indirect heat exchange with argon-containing fluid in the argon column top condenser to produce oxygen-containing gas; and (E) passing oxygen-containing gas into the lower pressure column for separation by cryogenic rectification.
Claim 2
Independent Claim
159 words
A method for the cryogenic rectification of feed air employing a double column main plant, comprising a higher pressure column and a lower pressure column, and an argon column having a top condenser, comprising: (A) condensing a portion of the feed air to produce liquid feed air; (B) passing liquid feed air and gaseous feed air into a stripping column and passing liquid feed air against gaseous feed air in the stripping column to produce stripping column product gas, having a nitrogen concentration which exceeds that of air, and stripping column product liquid, having an oxygen concentration which exceeds 25 mole percent; (C) passing stripping column product gas into the higher pressure column for separation by cryogenic rectification; (D) at least partially vaporizing stripping column product liquid by indirect heat exchange with argon-containing fluid in the argon column top condenser to produce oxygen-containing gas; and (E) passing oxygen-containing gas into the lower pressure column for separation by cryogenic rectification.
Claim 3
Dependent Claim
23 words
The method of claim 1 wherein the condensed feed air portion comprises from 20 to 45 percent of the total feed air employed.
Claim 4
Dependent Claim
25 words
The method of claim 1 wherein the feed air portion is condensed by indirect heat exchange with liquid oxygen taken from the lower pressure column.
Claim 5
Dependent Claim
20 words
The method of claim 1 wherein the gaseous feed air is turboexpanded prior to being passed into the stripping column.
Claim 6
Dependent Claim
34 words
The method of claim 1 further comprising passing a feed air stream in indirect heat exchange with liquid within the stripping column and thereafter passing said feed air stream into the lower pressure column.
Claim 7
Dependent Claim
27 words
The method of claim 1 wherein the stripping column product liquid is subcooled prior to being at least partially vaporized by indirect heat exchange with argon-containing fluid.
Claim 8
Dependent Claim
20 words
The method of claim 1 wherein the stripping column product liquid has an oxygen concentration which exceeds 33 mole percent.
Claim 9
Dependent Claim
41 words
The method of claim 1 further comprising recovering at least one of (i) product nitrogen taken from the lower pressure column, (ii) product oxygen taken from the lower pressure column, and (iii) product argon taken from the argon column top condenser.
Claim 10
Dependent Claim
104 words
A cryogenic rectification apparatus comprising: (A) a double column main plant comprising a first column and a second column, and an argon column having a top condenser; (B) a stripping column, means for passing liquid into the upper portion of the stripping column, and means for passing gas into the lower portion of the stripping column; (C) means for passing fluid from the upper portion of the stripping column into the first column; (D) means for passing fluid from the lower portion of the stripping column into the top condenser; and (E) means for passing fluid from the top condenser into the second column.
Claim 11
Dependent Claim
104 words
A cryogenic rectification apparatus comprising: (A) a double column main plant comprising a first column and a second column, and an argon column having a top condenser; (B) a stripping column, means for passing liquid into the upper portion of the stripping column, and means for passing gas into the lower portion of the stripping column; (C) means for passing fluid from the upper portion of the stripping column into the first column; (D) means for passing fluid from the lower portion of the stripping column into the top condenser; and (E) means for passing fluid from the top condenser into the second column.
Claim 12
Dependent Claim
51 words
The apparatus of claim 9 further comprising a product boiler, means for passing liquid from the second column into the product boiler, and means for passing liquid from the product boiler into the stripping column said means comprising the means for passing liquid into the upper portion of the stripping column.
Claim 13
Dependent Claim
21 words
The apparatus of claim 9 further comprising a turboexpander and means for passing gas from the turboexpander into the stripping column.
Claim 14
Dependent Claim
26 words
The apparatus of claim 9 wherein the means for passing fluid from the lower portion of the stripping column into the top condenser comprises a subcooler.
Claim 15
Dependent Claim
17 words
The apparatus of claim 9 wherein the mass transfer internals of the argon column comprise structured packing.
Claim 16
Dependent Claim
15 words
The apparatus of claim 13 wherein the argon column comprises at least 150 equilibrium stages.
Claim 17
Dependent Claim
13 words
The apparatus of claim 14 wherein the argon column is in two parts.
Claim 18
Dependent Claim
20 words
The apparatus of claim 9 wherein the stripping column and the first column are incorporated within the same column shell.
References Cited (Backward Citations)
US2316056A
Cited
US4737177A
Cited
US4715874A
Cited
US5019145A
Cited
US5098456A
Cited
US5108476A
Cited
US5114452A
Cited
US5114449A
Cited
US5291737A
Cited
US5265429A
Cited
US5245832A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1998-08-14 | 1999-02-13 | 1999-08-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2002-08-14 | 2003-02-13 | 2003-08-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2006-08-14 | 2007-02-13 | 2007-08-15 | $7700.00 | Window Closed / Lapsed |