US4303428A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Cryogenic processes for separating air
Assignee: LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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Filing: 1980-07-10
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Granted: 1981-12-01
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Expires: 2000-07-10
Abstract
Abstract This invention relates to cryogenic air separation processes. Liquid low-pressure oxygen is pumped to a high pressure and vaporized and heated in thermal exchange with a first high-pressure fluid, and a second intermediate-pressure fluid drawn off and expanded in a turbine. The invention is used in the production of oxygen under high pressure.
Inventors
- 👤 Gerard Vandenbussche
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 16:28
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04163; F25J3/04169; F25J3/04175; F25J3/04006; F25J3/04078; F25J3/0409; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04296; F25J3/04333; F25J3/04351; F25J3/04375; F25J3/04381; F25J3/04406; F25J3/04412; F25J2200/00; F25J2200/90; F25J2205/00; F25J2205/02; F25J2245/00; F25J2245/42
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
242 words
In a cryogenic process for separating air with the production of oxygen under high pressure, of the kind in which air is separated in a cryogenic separation apparatus comprising a medium-pressure upstream section and a low-pressure downstream section into at least one fraction rich in nitrogen and into at least one fraction rich in oxygen in the liquid state under low pressure, in which the said oxygen fraction is pumped in the liquid state from the said low pressure to the said high pressure, the said liquid oxygen fraction under high pressure being exposed to total vaporization by heat exchange in counterflow with fluids one of which is a first fluid which comprises at least one of the two principal components of air, and during the said exchange is under a high pressure of the order of the said high pressure, and is then expanded to the said medium pressure before being fed in an at least partially liquid state into at least one said separation section, and the other of which is a second fluid comprising air under an intermediate pressure greater than said medium pressure but also lower than said high pressure, and is fed in the gaseous state into said upstream separation section; the improvement in which an expansion of all of said second fluid to said medium pressure is carried out in turbine means at an intermediate temperature between the hot and cold temperature of said heat exchange.
Claim 2
Dependent Claim
242 words
In a cryogenic process for separating air with the production of oxygen under high pressure, of the kind in which air is separated in a cryogenic separation apparatus comprising a medium-pressure upstream section and a low-pressure downstream section into at least one fraction rich in nitrogen and into at least one fraction rich in oxygen in the liquid state under low pressure, in which the said oxygen fraction is pumped in the liquid state from the said low pressure to the said high pressure, the said liquid oxygen fraction under high pressure being exposed to total vaporization by heat exchange in counterflow with fluids one of which is a first fluid which comprises at least one of the two principal components of air, and during the said exchange is under a high pressure of the order of the said high pressure, and is then expanded to the said medium pressure before being fed in an at least partially liquid state into at least one said separation section, and the other of which is a second fluid comprising air under an intermediate pressure greater than said medium pressure but also lower than said high pressure, and is fed in the gaseous state into said upstream separation section; the improvement in which an expansion of all of said second fluid to said medium pressure is carried out in turbine means at an intermediate temperature between the hot and cold temperature of said heat exchange.
Claim 3
Dependent Claim
21 words
A process according to claim 1, wherein, after expansion, said first fluid is fed into said separation section under medium pressure.
Claim 4
Dependent Claim
22 words
A process according to claim 2, wherein said high pressure of said first fluid is substantially greater than said high oxygen pressure.
Claim 5
Dependent Claim
22 words
A process according to claim 2, wherein said high pressure of said first fluid is substantially lower than said high oxygen pressure.
Claim 6
Dependent Claim
22 words
A process according to claim 1, wherein said high pressure of said first fluid is substantially greater than said high oxygen pressure.
Claim 7
Dependent Claim
22 words
A process according to claim 1, wherein said high pressure of said first fluid is substantially lower than said high oxygen pressure.
Claim 8
Dependent Claim
12 words
A process according to claim 1, wherein said first fluid is air.
Claim 9
Dependent Claim
12 words
A process according to claim 1, wherein said first fluid is nitrogen.
Claim 10
Dependent Claim
15 words
A process according to claim 1, wherein said intermediate pressure is 8 to 20 bars.
Claim 11
Dependent Claim
14 words
A process according to claim 1, wherein said intermediate pressure is about 15 bars.
Claim 12
Dependent Claim
15 words
A process according to claim 1, wherein said high pressure is 15 to 100 bars.
Claim 13
Dependent Claim
15 words
A process according to claim 1, wherein said high pressure is 40 to 65 bars.
References Cited (Backward Citations)
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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) | 1984-11-30 | 1985-06-01 | 1985-12-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-11-30 | 1989-06-01 | 1989-12-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-11-30 | 1993-06-01 | 1993-12-01 | $7700.00 | Window Closed / Lapsed |