US4985052A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing high purity oxygen gas from air
Assignee: Bergwerksverband GmbH
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Filing: 1988-07-18
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Granted: 1991-01-15
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Expires: 2008-07-18
Abstract
Abstract 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.
Inventors
- 👤 Kazuo Haruna
- 👤 Kanji Ueda
- 👤 Masahiro Inoue
- 👤 Hitosi Someda
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 13:22
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: 3
Claim 1
Independent Claim
333 words
A process for producing high purity oxygen from air by PSA, with an apparatus comprising: a first adsorption unit packed with carbon molecular sieve; a second adsorption unit packed with zeolite molecular sieve connected in series with the first adsorption unit, each of the units being composed of two adsorbers, and a dehydrant being further packed in the gas inlet of each adsorber; one gas receiver provided between the first and second units for accumulating a desorption gas from the first adsorption unit as well as for introducing the desorption gas to the second unit as a raw material gas and to the first unit as a rinse gas; and one vacuum pump and one refrigerator-type drier at the outlet of the vacuum pump to remove water for desorbing water from each unit, comprising the steps of: conducting PSA operation separately in each of the units during the same operation cycle time, with effecting a pressure equalization in the first adsorption unit by connecting the adsorber wherein adsorption has been completed to the adsorber wherein desorption has been completed at the outlet thereof as well as effecting a pressure equalization in the second adsorption unit 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, returning a part of the oxygen product gas to the above adsorber of the second adsorption unit wherein desorption has been completed; accumulating the desorption gas from the first adsorption unit in the receiver and then introducing the resulting desorption gas to the second unit as a raw material gas and to the first unit as the rinse gas, the raw material gas of the second adsorption unit and the rinse gas being initially desorbed gas from the first adsorption unit having an oxygen content of at least 70%; and desorbing water from each unit under reduced pressure by the vacuum pump and condensed by cooling with the refrigerator-type drier.
Claim 2
Dependent Claim
333 words
A process for producing high purity oxygen from air by PSA, with an apparatus comprising: a first adsorption unit packed with carbon molecular sieve; a second adsorption unit packed with zeolite molecular sieve connected in series with the first adsorption unit, each of the units being composed of two adsorbers, and a dehydrant being further packed in the gas inlet of each adsorber; one gas receiver provided between the first and second units for accumulating a desorption gas from the first adsorption unit as well as for introducing the desorption gas to the second unit as a raw material gas and to the first unit as a rinse gas; and one vacuum pump and one refrigerator-type drier at the outlet of the vacuum pump to remove water for desorbing water from each unit, comprising the steps of: conducting PSA operation separately in each of the units during the same operation cycle time, with effecting a pressure equalization in the first adsorption unit by connecting the adsorber wherein adsorption has been completed to the adsorber wherein desorption has been completed at the outlet thereof as well as effecting a pressure equalization in the second adsorption unit 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, returning a part of the oxygen product gas to the above adsorber of the second adsorption unit wherein desorption has been completed; accumulating the desorption gas from the first adsorption unit in the receiver and then introducing the resulting desorption gas to the second unit as a raw material gas and to the first unit as the rinse gas, the raw material gas of the second adsorption unit and the rinse gas being initially desorbed gas from the first adsorption unit having an oxygen content of at least 70%; and desorbing water from each unit under reduced pressure by the vacuum pump and condensed by cooling with the refrigerator-type drier.
Claim 3
Dependent Claim
29 words
The process according to claim 1, further comprising the step of: periodically releasing carbon dioxide accumulated in the apparatus in the atmosphere through the outlet of the vacuum pump.
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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) | 1994-01-14 | 1994-07-16 | 1995-01-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-01-14 | 1998-07-16 | 1999-01-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-01-14 | 2002-07-16 | 2003-01-15 | $7700.00 | Window Closed / Lapsed |