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EP0302658A2 Expired / Lapsed EP ⏱️ 0.0 years remaining

Process for producing high purity oxygen gas from air

Assignee: Bergwerksverband GmbH
•
Filing: 1988-07-27
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Granted: —
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Expires: 2008-07-27
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Abstract

Abstract A process for producing a high purity oxygen from air by PSA comprises connecting a first adsorption unit 15A, 15B packed with carbon molecular sieve and a second adsorption unit 17A, 17B packed with zeolite molecular sieve in series, and conducting PSA operation separately in each of the units during the same operation cycle time. The desorption gas from the first adsorption unit 15A, 15B is accumulated in a receiver 16 and then introduced to the second unit 17A, 17B as a raw material gas and to the first unit 15A, 15B as a rinse gas.

Inventors

  • 👤 Kazuo Haruna
  • 👤 Kanji Ueda
  • 👤 Masahiro Inoue
  • 👤 Hitosi Someda

Bibliographic Details

Application Number —
Jurisdiction EP
Data Source google_patents
Last Synchronized 2026-10-27 08:06
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D53/0476; B01D2253/00; B01D2253/10; B01D2253/104; B01D2253/106; B01D2253/108; B01D2253/116; B01D2253/25; B01D2253/30; B01D2253/302; B01D2253/308; B01D2256/00; B01D2256/12; B01D2257/00; B01D2257/50; B01D2257/504; B01D2257/80; B01D2259/00; B01D2259/40; B01D2259/40001; B01D2259/40011; B01D2259/40013; B01D2259/40015; B01D2259/4002; B01D2259/40022; B01D2259/40028; B01D2259/4003; B01D2259/40035; B01D2259/40037; B01D2259/40043; B01D2259/4005; B01D2259/40052; B01D2259/40058; B01D2259/40066; B01D2259/40077; B01D2259/40081; B01D2259/402; B01D2259/414; B01D2259/4141; B01D2259/4145; B01D53/0473; B01D53/26; B01D53/261; Y; Y02; Y02C; Y02C20/00; Y02C20/40

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 88 words
A process for producing a high purity oxygen from air by PSA which comprises connecting a first adsorption unit packed with carbon molecular sieve and a second adsorption unit packed with zeolite molecular sieve in series, conducting PSA operation separately in each of the units during the same operation cycle time, accumulating the desorption gas from the first adsorption unit in a receiver and then introducing the resulting desorption gas to the second unit as a raw material gas and to the first unit as a rinse gas.
Claim 2
Dependent Claim 88 words
A process for producing a high purity oxygen from air by PSA which comprises connecting a first adsorption unit packed with carbon molecular sieve and a second adsorption unit packed with zeolite molecular sieve in series, conducting PSA operation separately in each of the units during the same operation cycle time, accumulating the desorption gas from the first adsorption unit in a receiver and then introducing the resulting desorption gas to the second unit as a raw material gas and to the first unit as a rinse gas.
Claim 3
Dependent Claim 59 words
The process according to claim 1, wherein a dehydrant is further packed in the gas inlet of each adsorber of the first and second units to adsorb water, and water is desorbed therefrom under reduced pressure by a vacuum pump and condensed by cooling with a refrigerator-­type drier provided at the outlet of the vacuum pump to remove water.
Claim 4
Dependent Claim 118 words
The process according to claim1,or claim 2 wherein the first adsorption unit packed with carbon molecular sieve is composed of two adsorbers and pressure equalization is effected by connecting the adsorber wherein adsorption has been completed to the adsorber wherein desorption has been completed at the outlet thereof, the second adsorption unit packed with zeolite molecular sieve is composed of two adsorbers and pressure equalization is effected by connecting the outlet of the adsorber wherein adsorption has been completed to the inlet of the adsorber wherein desorption has been completed, and, at the same time, a part of the oxygen product gas is returned to the above adsorber of the second adsorption unit wherein desorption has been completed.
Claim 5
Dependent Claim 31 words
The process according to any one of the preceding claims wherein carbon dioxide accumulated in the system is periodically released in the atmosphere through the outlet of the vacuum pump used.
Claim 6
Dependent Claim 51 words
The process according to any one of the preceding claims wherein initially desorbed gas from the first adsorption unit, which has oxygen content of 70% or more, is used as the raw material gas of the second adsorption unit and is used as the rinse gas of the first adsorption unit.
Claim 7
Independent Claim 75 words
An apparatus for producing a high purity oxygen from air by PSA said apparatus comprising a first adsorption unit packed with carbon molecular sieve and a second adsorption unit packed with zeolite molecular sieve, said first and second units being connected in series; and a receiver arranged to be connectable to said units and which is capable of receiving gas from said first unit and of releasing gas into said first and said second units.
Claim 8
Independent Claim 75 words
An apparatus for producing a high purity oxygen from air by PSA said apparatus comprising a first adsorption unit packed with carbon molecular sieve and a second adsorption unit packed with zeolite molecular sieve, said first and second units being connected in series; and a receiver arranged to be connectable to said units and which is capable of receiving gas from said first unit and of releasing gas into said first and said second units.
Claim 9
Dependent Claim 46 words
An apparatus according to claim 6 wherein the first adsorption unit comprises two adsorbers packed with carbon molecular sieve and the second adsorption unit comprises two adsorbers packed with zeolite molecular sieve adsorbers of each adsorption unit being connectable to each other for effecting pressure equalisation.
Claim 10
Dependent Claim 46 words
An apparatus according to claim 6 or claim 7 wherein adsorbers of said adsorption units are each provided with an inlet which contains a dehydrant and wherein outlets of said adsorbers are operably connected to a vacuum pump having a refrigerator type drier at its outlet.

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