Patent US4575388A successfully refreshed from Google Patents.
US4575388A
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Process for recovering argon
Assignee: Taiyo Nippon Sanso Corp
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Filing: 1984-02-08
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Granted: 1986-03-11
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Expires: 2004-02-08
Abstract
Abstract A process for recovering argon in which a crude argon column is supplied with an argon feed gas containing a larger proportion of oxygen from a double rectifier and is cooled at its head portion with or without liquid air from a sump of the lower column of the double rectifier for producing a reflux of argon in the crude argon column. In the process, argon gas is compressed to a pressure sufficient for evaporating liquid oxygen fed from a condenser of the double rectifier, is then precooled in a heat exchanger, and thereafter liquefied by heat exchange with the liquid oxygen. Then the head portion of the crude argon column is cooled with the liquefied argon, which is then returned in a gaseous state for further compression to thereby circulate the argon gas.
Inventors
- 👤 Hidetake Okada
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 15:11
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04248; F25J3/04333; F25J3/04351; F25J3/04278; F25J3/04284; F25J3/0429; F25J3/04303; F25J3/04369; F25J3/04406; F25J3/04412; F25J3/04642; F25J3/04648; F25J3/04654; F25J3/04666; F25J3/04672; F25J3/04678; F25J3/04763; F25J3/04866; F25J3/04969; F25J2235/00; F25J2235/58; F25J2245/00; F25J2245/58; F25J2250/00; F25J2250/20; F25J2270/00; F25J2270/58; Y; Y10; Y10S; Y10S62/00; Y10S62/923; Y10S62/924
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
169 words
In a process for recovering argon in which a crude argon column is supplied with an argon feed gas containing a larger proportion of oxygen from a middle stage of an upper column of a double rectification column for low temperature air separation, the improvement comprising retrofitting an existing process to maximize argon recovery and minimize power consumption while precluding deterioration of rectification conditions in the upper column including the steps of: (a) compressing argon gas to a pressure sufficient for evaporating liquid oxygen fed from a condenser of the double rectification column; (b) precooling the compressed argon gas in a heat exchanger; (c) liquefying the precooled argon gas by heat exchange with liquid oxygen from the condenser of the double rectification column; (d) introducing the liquefied argon as a reflux into the head portion of the crude argon column thereby cooling said head portion and evaporating the liquefied argon; and (e) returning the evaporated argon to the step (a) for further compression to thereby circulate the argon gas.
Claim 2
Dependent Claim
169 words
In a process for recovering argon in which a crude argon column is supplied with an argon feed gas containing a larger proportion of oxygen from a middle stage of an upper column of a double rectification column for low temperature air separation, the improvement comprising retrofitting an existing process to maximize argon recovery and minimize power consumption while precluding deterioration of rectification conditions in the upper column including the steps of: (a) compressing argon gas to a pressure sufficient for evaporating liquid oxygen fed from a condenser of the double rectification column; (b) precooling the compressed argon gas in a heat exchanger; (c) liquefying the precooled argon gas by heat exchange with liquid oxygen from the condenser of the double rectification column; (d) introducing the liquefied argon as a reflux into the head portion of the crude argon column thereby cooling said head portion and evaporating the liquefied argon; and (e) returning the evaporated argon to the step (a) for further compression to thereby circulate the argon gas.
Claim 3
Dependent Claim
100 words
A process for recovering argon as recited in claim 1, further comprising the steps of: (f) before the compression step (a), introducing the argon gas issuing from the head of the crude argon column into the heat exchanger for precooling the compressed argon gas by heat exchange therewith; (g) sending the argon gas, which is introduced into the heat exchanger and heat exchanged therein in the step (f), to the compressing step (a); and (h) subsequently to the compressing step (a), delivering part of the compressed argon gas for further purification thereof and the rest to the precooling step (b).
Claim 4
Dependent Claim
28 words
A process for recovering argon as recited in claim 2, further comprising the step of pumping the argon liquified in the step (c) to the cooling step (d).
References Cited (Backward Citations)
US4384876A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-03-10 | 1989-09-09 | 1990-03-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-03-10 | 1993-09-09 | 1994-03-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-03-10 | 1997-09-09 | 1998-03-11 | $7700.00 | Window Closed / Lapsed |