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US5203887A Expired / Lapsed US ⏱️ 0.0 years remaining

Adsorbent beds for pressure swing adsorption operations

Assignee: Praxair Technology Inc
•
Filing: 1991-12-11
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Granted: 1993-04-20
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Expires: 2011-12-11
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Abstract

Abstract Composite adsorbent beds comprised of conventional 13X adsorbent and special cation exchanged adsorbent materials enable vacuum pressure swing adsorption operations for air separation to be carried out at advantageously low oxygen or nitrogen product costs.

Inventors

  • 👤 Lee J. Toussaint

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 21:17
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D53/0476; B01J; B01J20/00; B01J20/02; B01J20/10; B01J20/16; B01J20/18; B01D2253/00; B01D2253/10; B01D2253/104; B01D2253/106; B01D2253/108; B01D2253/1085; B01D2256/00; B01D2256/10; B01D2256/12; B01D2259/00; B01D2259/40; B01D2259/402; B01D2259/416; Y; Y10; Y10S; Y10S95/00; Y10S95/90; Y10S95/902

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 186 words
In a vacuum pressure swing adsorption system for the recovery of oxygen or nitrogen from air, said system being adapted to operate between a superatmospheric or atmospheric higher adsorption pressure and a subatmospheric lower desorption pressure on a cycle basis, said system containing one or more adsorbent bed, each bed being capable of selectively adsorbing nitrogen as the more readily adsorbable component of feed air, the improvement comprising incorporating, as each said adsorbent bed, a composite bed comprising special adsorbent material at the feed end of the bed and conventional non-ion-exchanged zeolite X adsorbent material at the opposite, product end thereof, said special adsorbent material extending from said feed end comprising from about 25% to about 95% of the overall adsorbent bed, said special adsorbent material comprising the lithium cation form of zeolite X in which the Si/Al 2 molar ratio is from about 2.0 to about 3.0 and in which at least about 88% of the AlO 2 -tetrahedral units are associated with lithium cations, whereby the product costs are desirably reduced, without any appreciable increase in power requirements, compared to an all-special adsorbent system.
Claim 2
Dependent Claim 186 words
In a vacuum pressure swing adsorption system for the recovery of oxygen or nitrogen from air, said system being adapted to operate between a superatmospheric or atmospheric higher adsorption pressure and a subatmospheric lower desorption pressure on a cycle basis, said system containing one or more adsorbent bed, each bed being capable of selectively adsorbing nitrogen as the more readily adsorbable component of feed air, the improvement comprising incorporating, as each said adsorbent bed, a composite bed comprising special adsorbent material at the feed end of the bed and conventional non-ion-exchanged zeolite X adsorbent material at the opposite, product end thereof, said special adsorbent material extending from said feed end comprising from about 25% to about 95% of the overall adsorbent bed, said special adsorbent material comprising the lithium cation form of zeolite X in which the Si/Al 2 molar ratio is from about 2.0 to about 3.0 and in which at least about 88% of the AlO 2 -tetrahedral units are associated with lithium cations, whereby the product costs are desirably reduced, without any appreciable increase in power requirements, compared to an all-special adsorbent system.
Claim 3
Dependent Claim 24 words
The system of claim 1 in which the bed fraction of special adsorbent material is about 50% to about 75% of the total bed.
Claim 4
Dependent Claim 13 words
The system of claim 1 in which said conventional adsorbent material comprises 13X.
Claim 5
Dependent Claim 25 words
The system of claim 3 in which said special adsorbent material has at least 90% of the AlO 2 -tetrahedral units associated with lithium cations.
Claim 6
Dependent Claim 21 words
The system of claim 4 in which at least 95% of the AlO 2 -tetrahedral units are associated with lithium cations.
Claim 7
Dependent Claim 28 words
The system of claim 5 in which the special adsorbent material at the feed end of the bed comprises about 50% to about 75% of the total bed.
Claim 8
Dependent Claim 13 words
The system of claim 6 in which said system comprises two adsorbent beds.
Claim 9
Dependent Claim 13 words
The system of claim 3 in which said system comprises two adsorbent beds.
Claim 10
Dependent Claim 15 words
The system of claim 1 in which the system is adapted to produce oxygen product.
Claim 11
Dependent Claim 25 words
The system of claim 9 in which the system is adapted to produce oxygen product having a purity of from about 88% to about 93%.
Claim 12
Dependent Claim 15 words
The system of claim 1 in which said system is adapted to produce nitrogen product.
Claim 13
Dependent Claim 54 words
The system of claim 1 and including a conventional non-ion-exchanged zeolite X adsorbent material at the feed end of the bed upstream of said composite bed of special adsorbent material and conventional adsorbent material, said special adsorbent material forming an intermediate portion of said bed between the conventional adsorbent material at each end thereof.
Claim 14
Dependent Claim 32 words
The system of claim 12 in which the conventional adsorbent at the feed end of the bed has a bed fraction of from about 5% to about 30% of the total bed.
Claim 15
Dependent Claim 12 words
The system of claim 13 in which said conventional adsorbent comprises 13X.
Claim 16
Dependent Claim 22 words
The system of claim 14 in which at least about 95% of the AlO 1 -tetrahedral units are associated with lithium cations.
Claim 17
Dependent Claim 12 words
The system of claim 12 in which said conventional adsorbent comprises 13X.
Claim 18
Dependent Claim 13 words
The system of claim 12 in which said system comprises two adsorbent beds.
Claim 19
Dependent Claim 13 words
The system of claim 1 in which said system comprises two adsorbent beds.

References Cited (Backward Citations)

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