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US3100696A Expired / Lapsed US ⏱️ 0.0 years remaining

Method and apparatus for separating gases

Assignee: Linde GmbH
•
Filing: 1959-06-08
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Granted: 1963-08-13
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Expires: 1979-06-08
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Abstract

Abstract 900,438. Cold separation of gas mixtures. LINDE'S EISMASCHINEN A.G. GES. FUR. June 10, 1959 [June, 11, 1958], No. 19872/59. Class 8(2). In a gas mixture e.g. air rectification process wherein incoming compressed air is cooled in pairs of nitrogen regenerators 1, 2, Fig. 1, and oxygen regenerators 4, 5 and wherein a portion of the cooled air is reheated by passing it through an additional regenerator e.g. a nitrogen regenerator 3 at least part of said reheated air is cooled in a counter current heat exchanger 15 traversed by cold nitrogen product which is discharged through a line 18 at substantially ambient temperature; the so-cooled portion of the re-heated air being added to the main flow of air entering the column 8 at a point 7 whilst the remainder of the re-heated air is fed to the. low pressure section of the column preferably after expansion in a turbine 12. Regenerators 1, 2 are supplied with slightly impure nitrogen from a point 13 and regenerators 4, 5 are supplied with gaseous oxygen from a point 9; product liquid oxygen being with-drawn through a duct 19. In a modification an additional regenerator 2<SP>1</SP>, Fig. 2, is connected in parallel to regenerator 2, cold air to be re-heated in regenerator 3 is withdrawn from a point 20 at the cold end of regenerator 1, 2 the re-heated air leaving the top of regenerator 3 through a line 22 is cooled in exchanger 15 before combining with that in a line 11 and traversing a gel absorber 24 and a further exchanger 15<SP>1</SP> the exchangers 15, 15<SP>1</SP> being traversed by nitrogen from an auxiliary column 25 interposed between the low and high pressure sections of the column 8.

Inventors

  • 👤 Becker Rudolf

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 17:46
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04242; F25J3/04248; F25J3/04284; F25J3/0429; F25J3/04303; F25J3/04333; F25J3/04339; F25J3/04406; F25J3/04412; F25J3/04436; F25J3/04448; F25J2205/00; F25J2205/24; F25J2205/30; F25J2205/60; F25J2290/00; F25J2290/10; Y; Y10; Y10S; Y10S62/00; Y10S62/902; Y10S62/908; Y10S62/909

Claims Analysis

Total Claims: 1
Claim 1
Independent Claim 123 words
IN THE PROCESS FOR THE SEPARATION OF A GAS MIXTURE INTO A HIGHER BOILING POINT FRACTION AND AT LEAST ONE FRACTION OF LOWER BOILING POINT, THE METHOD WHICH COMPRISES COMPRESSING THE GAS MIXTURE, COOLING AND PURIFYING THE COMPRESSED GAS MIXTURE IN AT LEAST ONE REGENERATOR OF A REVERSING REGENERATOR SYSTEM, FEEDING A FIRST PART OF THE COOLEC COMPRESSED GAS MIXTURE INTO A RECITFYING DEVICE, PASSING A SECOND PART OF THE COOLED COMPRESSED GAS MIXTURE IN THE OPPOSITE DIRECTION THROUGH A SECOND REGENERATOR, WARMING THIS SECOND PART THEREBY AT LEAST PARTIALLY TO AMBIENT TEMPERATURE, COOLING SAID WARMED SECOND PART OF THE GAS MIXTURE BY HEAT EXCHANGE WITH AT LEAST PART OF A SEPARATION PRODUCT WITHDRAWN FROM THE RECTIFYING DEVICE, WARMING SAID SEPARATION PRODUCT THERE-

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1966-08-12 1967-02-11 1967-08-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1970-08-12 1971-02-11 1971-08-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1974-08-12 1975-02-11 1975-08-13 $7700.00 Window Closed / Lapsed

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