US5265429A
Expired / Lapsed
US
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Cryogenic air separation system for producing gaseous oxygen
Assignee: Praxair Technology Inc
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Filing: 1992-02-21
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Granted: 1993-11-30
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Expires: 2012-02-21
Abstract
Abstract A cryogenic air separation system employing a product boiler coupled with a liquid air supply whereby liquid oxygen is effectively vaporized to produce gaseous oxygen product while providing for steady state operation of the cryogenic air separation plant without significant refrigeration loss.
Inventors
- 👤 James R. Dray
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 12:26
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04406; F25J3/04412; F25J3/04006; F25J3/04078; F25J3/0409; F25J3/04151; F25J3/04187; F25J3/04193; F25J3/04206; F25J3/0423; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04296; F25J3/04472; F25J3/04496; F25J3/04503; F25J3/04509; F25J3/04515; F25J3/04642; F25J3/04648; F25J3/04654; F25J3/04666; F25J3/04672; F25J3/04678; F25J2205/00; F25J2205/02; F25J2250/00; F25J2250/30; F25J2250/40; F25J2250/50; F25J2250/58; Y; Y10; Y10S; Y10S62/00; Y10S62/923; Y10S62/924; Y10S62/939; Y10S62/94
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
233 words
A method for producing gaseous oxygen by the cryogenic rectification of feed air comprising: (A) passing a fraction of the feed air into a product boiler and condensing feed air by indirect heat exchange with liquid oxygen in the product boiler; (B) passing condensed feed air into a cryogenic rectification plant comprising a higher pressure column and a lower pressure column and producing liquid oxygen therein; (C) passing liquid oxygen produced in the cryogenic rectification plant to the product boiler to carry out the condensation of the feed air, and recovering gaseous oxygen from the product boiler as product; (D) pumping liquid oxygen produced in the cryogenic rectification plant and thereafter passing the pumped liquid oxygen into a liquid oxygen tank to produce a supply of liquid oxygen; (E) increasing the flow of liquid oxygen to the product boiler by passing liquid oxygen from the liquid oxygen supply to the product boiler and commensurately increasing the flow of feed air to the product boiler to produce excess condensed feed air; (F) passing excess condensed feed air produced in the product boiler into a liquid air tank to produce a supply of liquid air while continuing to pass condensed feed air into the cryogenic rectification plant without passing through the liquid air tank; and (G) turboexpanding another fraction of the feed air and passing the turboexpanded feed air fraction into the higher pressure column.
Claim 2
Independent Claim
233 words
A method for producing gaseous oxygen by the cryogenic rectification of feed air comprising: (A) passing a fraction of the feed air into a product boiler and condensing feed air by indirect heat exchange with liquid oxygen in the product boiler; (B) passing condensed feed air into a cryogenic rectification plant comprising a higher pressure column and a lower pressure column and producing liquid oxygen therein; (C) passing liquid oxygen produced in the cryogenic rectification plant to the product boiler to carry out the condensation of the feed air, and recovering gaseous oxygen from the product boiler as product; (D) pumping liquid oxygen produced in the cryogenic rectification plant and thereafter passing the pumped liquid oxygen into a liquid oxygen tank to produce a supply of liquid oxygen; (E) increasing the flow of liquid oxygen to the product boiler by passing liquid oxygen from the liquid oxygen supply to the product boiler and commensurately increasing the flow of feed air to the product boiler to produce excess condensed feed air; (F) passing excess condensed feed air produced in the product boiler into a liquid air tank to produce a supply of liquid air while continuing to pass condensed feed air into the cryogenic rectification plant without passing through the liquid air tank; and (G) turboexpanding another fraction of the feed air and passing the turboexpanded feed air fraction into the higher pressure column.
Claim 3
Dependent Claim
38 words
The method of claim 1 further comprising passing an argon-containing fluid from the cryogenic rectification plant into an argon column and recovering an argon fluid having an argon concentration of at least 95 percent from the argon column.
Claim 4
Dependent Claim
199 words
A cryogenic air separation plant for producing gaseous oxygen comprising: (A) a product boiler, means for supplying feed air to the product boiler, and means for passing liquid from the product boiler to a cryogenic rectification plant comprising a higher pressure column and a lower pressure column; (B) means for passing liquid from the cryogenic rectification plant into the product boiler and means for recovering gaseous product from the product boiler; (C) a liquid oxygen tank, a pump, means for passing liquid from the cryogenic rectification plant to the pump and from the pump into the liquid oxygen tank, and means for passing liquid from the liquid oxygen tank into the product boiler; (D) a liquid air tank, means for passing liquid from the product boiler into the liquid air tank, and means for passing liquid from the liquid air tank into the cryogenic rectification plant and wherein the said means for passing liquid from the product boiler to the cryogenic rectification plant in clause (A) does not include the liquid air tank; and (E) a turboexpander, means for passing feed air into the turboexpander, and means for passing feed air from the turboexpander into the higher pressure column.
Claim 5
Dependent Claim
199 words
A cryogenic air separation plant for producing gaseous oxygen comprising: (A) a product boiler, means for supplying feed air to the product boiler, and means for passing liquid from the product boiler to a cryogenic rectification plant comprising a higher pressure column and a lower pressure column; (B) means for passing liquid from the cryogenic rectification plant into the product boiler and means for recovering gaseous product from the product boiler; (C) a liquid oxygen tank, a pump, means for passing liquid from the cryogenic rectification plant to the pump and from the pump into the liquid oxygen tank, and means for passing liquid from the liquid oxygen tank into the product boiler; (D) a liquid air tank, means for passing liquid from the product boiler into the liquid air tank, and means for passing liquid from the liquid air tank into the cryogenic rectification plant and wherein the said means for passing liquid from the product boiler to the cryogenic rectification plant in clause (A) does not include the liquid air tank; and (E) a turboexpander, means for passing feed air into the turboexpander, and means for passing feed air from the turboexpander into the higher pressure column.
Claim 6
Dependent Claim
35 words
The cryogenic air separation plant of claim 3 further comprising an argon column, means for passing fluid from the cryogenic rectification plant into the argon column, and means for recovering fluid from the argon column.
Claim 7
Dependent Claim
30 words
The method of claim 1 further comprising cooling condensed feed air by indirect heat exchange with liquid oxygen prior to passing the condensed feed air into the cryogenic rectification plant.
Claim 8
Dependent Claim
39 words
The cryogenic air separation plant of claim 3 further comprising a heat exchanger, means for passing liquid from the product boiler to the heat exchanger, and means for passing liquid from the heat exchanger into the cryogenic rectification plant.
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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) | 1996-11-29 | 1997-05-31 | 1997-11-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-11-29 | 2001-05-31 | 2001-11-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-11-29 | 2005-05-31 | 2005-11-30 | $7700.00 | Window Closed / Lapsed |