Patent US4555256A successfully refreshed from Google Patents.
US4555256A
Expired / Lapsed
US
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Process and device for the production of gaseous oxygen at elevated pressure
Assignee: Linde GmbH
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Filing: 1983-05-02
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Granted: 1985-11-26
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Expires: 2003-05-02
Abstract
Abstract In the production of gaseous oxygen, a process and apparatus is used which requires low temperature rectification of air. The air is compressed, purified and cooled in a first heat exchanger while a second gas stream is compressed to elevated pressure, and is cooled in a second heat exchanger. Liquid oxygen removed from rectification is pressurized to a desired pressure and is evaporated and heated in heat exchange with the compressed gas stream.
Inventors
- 👤 Werner Skolaude
- 👤 Gunnar Eggendorfer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 16:15
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04187; F25J3/04218; F25J3/04006; F25J3/04078; F25J3/0409; F25J3/04157; F25J3/04224; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04296; F25J3/04303; F25J3/04333; F25J3/04339; F25J3/04345; F25J3/04351; F25J3/04357; F25J3/04375; F25J3/04387; F25J3/04393; F25J3/04406; F25J3/04412; F25J2205/00; F25J2205/30; F25J2205/32; F25J2240/00; F25J2240/02; F25J2240/10; F25J2245/00; F25J2245/02; F25J2245/40; Y; Y10; Y10S; Y10S62/00; Y10S62/939; Y10S62/94
Claims Analysis
Total Claims: 25
Claim 1
Independent Claim
200 words
Process for the production of gaseous O at an elevated pressure by low temperature rectification of air, comprising reducing energy requirements for production of oxygen by compressing, purifying and at least in part cooling the air in a first heat exchange in heat exchange with rectification product, passing the air to the rectification, compressing a second gas stream to a higher pressure, cooling the second gas stream, after compressing, in a second heat exchanger in heat exchange with rectification product, withdrawing heat at an intermediate point along the second heat exchanger, whereby temperature differences at a cold end of the second heat exchanger are reduced, adding the withdrawn heat to the first heat exchanger, whereby less air is required for heating at a cold end of the first heat exchanger, expanding the second gas stream, after cooling, and passing the second gas stream, after expanding to the rectification, and cooling a third gas stream to be fractionated in heat exchange with fractionation product, liquid oxygen being withdrawn from the rectification, and being pumped to the desired pressure, and, in heat exchange with the compressed gas stream, being evaporated and heated, whereby energy requirements for the production of oxygen is reduced.
Claim 2
Dependent Claim
200 words
Process for the production of gaseous O at an elevated pressure by low temperature rectification of air, comprising reducing energy requirements for production of oxygen by compressing, purifying and at least in part cooling the air in a first heat exchange in heat exchange with rectification product, passing the air to the rectification, compressing a second gas stream to a higher pressure, cooling the second gas stream, after compressing, in a second heat exchanger in heat exchange with rectification product, withdrawing heat at an intermediate point along the second heat exchanger, whereby temperature differences at a cold end of the second heat exchanger are reduced, adding the withdrawn heat to the first heat exchanger, whereby less air is required for heating at a cold end of the first heat exchanger, expanding the second gas stream, after cooling, and passing the second gas stream, after expanding to the rectification, and cooling a third gas stream to be fractionated in heat exchange with fractionation product, liquid oxygen being withdrawn from the rectification, and being pumped to the desired pressure, and, in heat exchange with the compressed gas stream, being evaporated and heated, whereby energy requirements for the production of oxygen is reduced.
Claim 3
Dependent Claim
17 words
Process according to claim 1, characterized in that the third gas stream is further compressed before cooling.
Claim 4
Dependent Claim
28 words
Process according to claim 1, characterized in that the third gas stream after expansion is passed either to the rectification or into nitrogen, drawn off from the rectification.
Claim 5
Dependent Claim
26 words
Process according to claim 1, characterized in that the third gas stream is removed from first heat exchanger, essentially at the point where heat is added.
Claim 6
Dependent Claim
15 words
Process according to claim 1, characterized in that the second partial stream is engine expanded.
Claim 7
Dependent Claim
48 words
Process according to claim 1, characterized in that for heat transfer purposes, a portion of the second compressed gas stream, before cooling is complete, is cooled in heat exchange with a portion of gas stream from the rectification, which is to be heated in the first heat exchanger.
Claim 8
Dependent Claim
50 words
Process according to claim 1, characterized in that the compression of the second gas stream occurs in two steps, whereby between the two steps a partial stream branches off, is cooled in a second heat exchanger and before heat exchange is completed, is engine expanded and passed into the rectification.
Claim 9
Dependent Claim
35 words
Process according to claim 1, characterized in that a portion of second gas stream, compressed to its final pressure, branches off before completion of the heat exchange, is engine expanded and passed into the rectification.
Claim 10
Dependent Claim
53 words
Process according to claim 1, characterized in that nitrogen from the rectification, is passed through the first and the second heat exchanger, in part, respectively, and a portion of the nitrogen is transferred from an intermediate point of the second heat exchanger to the nitrogen at an intermediate point of first heat exchanger.
Claim 11
Dependent Claim
31 words
Process according to claim 1, characterized in that the second gas stream is a partial stream of the air to be fractionated or a gas stream from the high pressure stage.
Claim 12
Dependent Claim
26 words
Process according to claim 1, characterized in that the power gained in the expansion of the second and/or third gas stream is used for its compression.
Claim 13
Dependent Claim
92 words
Process according to claim 1, characterized in that a portion of the second gas stream is used as the third partial stream, whereby the second gas stream is split into first and second partial streams, which are cooled in the second heat exchanger, separate from each other, at different pressures, and in that a partial stream having the lower pressure, is removed from the second heat exchanger at a higher temperature than the higher compressed second partial stream, thereupon is engine expanded and, at least in part, is passed to the rectification.
Claim 14
Dependent Claim
21 words
Process according to claim 12, characterized in that the second partial stream, being at elevated pressure, is engine expanded after cooling.
Claim 15
Dependent Claim
27 words
Process according to claim 12, characterized in that the first partial stream, being at lower pressure, after exiting from the first compression stage, is after-compressed before cooling.
Claim 16
Dependent Claim
25 words
Process according to claim 12, characterized in that the pressure of the first partial stream, having the lower pressure, ranges between 10 and 60 bar.
Claim 17
Dependent Claim
42 words
Process according to claim 12, characterized in that the first partial stream, having the lower pressure, is withdrawn from the second heat exchanger in the area of the smallest temperature differential between the second partial stream, having the higher pressure, and oxygen.
Claim 18
Dependent Claim
31 words
Process according to claim 12, characterized in that the output realized in the expansion of one or both partial streams is utilized for the after-compression of one or both partial streams.
Claim 19
Dependent Claim
28 words
Process according to claim 12, characterized in that heat is transferred from an intermediate point of one heat exchanger to an intermediate point of the other heat exchanger.
Claim 20
Dependent Claim
35 words
Process according to claim 12, characterized in that a portion of the compressed, purified air is branched off at an intermediate point of the first heat exchanger, is engine expanded and passed into the rectification.
Claim 21
Dependent Claim
18 words
Process according to claim 19, characterized in that the branched off portion of air is after-compressed before cooling.
Claim 22
Dependent Claim
20 words
Process according to claim 12, characterized in that the second gas stream is a partial stream of the incoming air.
Claim 23
Dependent Claim
25 words
Process according to claim 12, characterized in that the second gas stream is withdrawn from pressure stage and is heated and compressed before the splitting.
Claim 24
Dependent Claim
45 words
Process according to claim 22, characterized in that before compression of the second gas stream, a portion is branched off and is after-compressed, cooled in one of the heat exchangers, is withdrawn therefrom at an intermediate point, is engine expanded and passed into the rectification.
Claim 25
Dependent Claim
43 words
Process according to claim 1, characterized in that as said third gas stream a portion of the compressed purified air is cooled in the first heat exchanger, then is removed at least in part, at an intermediate point therefrom, and is engine expanded.
References Cited (Backward Citations)
US4372764A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-11-25 | 1989-05-27 | 1989-11-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-11-25 | 1993-05-27 | 1993-11-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-11-25 | 1997-05-27 | 1997-11-26 | $7700.00 | Window Closed / Lapsed |