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Process and apparatus for the low-temperature separation of air

Assignee: Linde GmbH
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Filing: 1976-08-06
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Granted: 1978-05-30
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Expires: 1996-08-06
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Abstract

Abstract In a process for the low-temperature separation of air into dry product gases wherein at least a portion of the entering air is cooled by indirect heat exchange in a heat exchanger against at least one of the product gases and is freed of impurities by an adsorption process prior to this heat exchange, the improvement which comprises freeing the air of substantially only H 2 O in the adsorption process and periodically interchanging the flow paths for the air and for the product gas, respectively, in the heat-exchanger.

Inventors

  • 👤 Wilhelm Rohde

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 12:44
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04151; F25J3/04163; F25J3/04169; F25J2205/00; F25J2205/24

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 115 words
In a process for the low-temperature separation of air into dry product gases wherein the entering air is divided into two portions, one portion being freed of impurities in an adsorption process and being then cooled by indirect heat exchange in a secondary heat exchanger against oxygen product gas and the other portion being cooled in a primary heat exchanger directly without an intermediate adsorption treatment, the improvement which comprises freeing said one portion of the air of substantially only H 2 O in the adsorption process by passing the air over a dry gel desiccant and periodically interchanging the flow paths for the air and for the oxygen product gas, respectively, in the heat-exchanger.
Claim 2
Dependent Claim 115 words
In a process for the low-temperature separation of air into dry product gases wherein the entering air is divided into two portions, one portion being freed of impurities in an adsorption process and being then cooled by indirect heat exchange in a secondary heat exchanger against oxygen product gas and the other portion being cooled in a primary heat exchanger directly without an intermediate adsorption treatment, the improvement which comprises freeing said one portion of the air of substantially only H 2 O in the adsorption process by passing the air over a dry gel desiccant and periodically interchanging the flow paths for the air and for the oxygen product gas, respectively, in the heat-exchanger.
Claim 3
Dependent Claim 13 words
A process according to claim 1 wherein the secondary heat exchanger comprises regenerators.
Claim 4
Dependent Claim 51 words
A process according to claim 1 wherein the interchanging of the flow paths comprises more than two flow conduits which are cylically switched over so that in each case a number of conduits is utilized for the product gas and a smaller number of conduits is used for the inlet air.
Claim 5
Dependent Claim 16 words
A process according to claim 1, wherein said dry gel is activated alumina or silica gel.
Claim 6
Dependent Claim 22 words
A process according to claim 1, wherein said adsorption process comprises parallel interchangeable adsorbers and said adsorbers are regenerated with hot air.
Claim 7
Dependent Claim 15 words
A process according to claim 5, wherein the adsorber contains silica gel or activated alumina.

References Cited (Backward Citations)

US2699837A Cited
US3210950A Cited
US3280574A Cited
US3355859A Cited
US3967464A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-05-29 1981-11-28 1982-05-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-05-29 1985-11-28 1986-05-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-05-29 1989-11-28 1990-05-30 $7700.00 Window Closed / Lapsed

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