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US4943304A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the purification of bulk gases using chabazite adsorbents

Assignee: Air Products and Chemicals Inc
•
Filing: 1989-04-06
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Granted: 1990-07-24
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Expires: 2009-04-06
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Abstract

Abstract A process is provided for the selective adsorption of one or more minor constituents from a bulk gas stream using a chabazite in which the bulk gas is size excluded from the pore structure of the chabazite or the minor constituent to be separated has a heat of adsorption greater than that of the bulk gas and the process is carried out under conditions such that the partial pressure of the minor constituent is in the linear low pressure region of the isotherm for the minor constituent and the adsorbent is a dehydrated divalent cation-containing chabazite having a Si/Al ratio of 1.8 to 2.7, a cation sitting, f s , of 0.7 to 1, and a cation distribution, f d , of 0.62 to 1.

Inventors

  • 👤 Charles G. Coe
  • 👤 Thomas R. Gaffney

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 23:11
CPC Classifications
C; C01; C01B; C01B23/00; B; B01; B01J; B01J20/00; B01J20/02; B01J20/10; B01J20/16; B01J20/18; C01B3/00; C01B3/50; C01B3/56; C01B2203/00; C01B2203/04; C01B2203/042; C01B2203/043; C01B2203/0465; C01B2203/047; C01B2203/048; Y; Y10; Y10S; Y10S95/00; Y10S95/90; Y10S95/902

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 146 words
In a process for the selective adsorption of one or more minor constituents from a bulk gas stream with a chabazite in which the bulk gas is size excluded from the pore structure of the chabazite or the minor constituted to be separated has a heat of adsorption greater than the bulk gas, the improvement which comprises separating the minor constituents utilizing a dehydrated calcium-exchanged chabazite having a Si/Al ratio of 1.9 to 2.3, a cation siting value f s , of about 0.9 to 1, a cation distribution value, f d , of about 0.74 to 1 and an adsorption capacity, C v , of at least about 40 cc N 2 /g at 30 ° C. and 1 atm under conditions such that the partial pressure of the minor constituent is in the linear low pressure region of the isotherm for the minor constituent.
Claim 2
Dependent Claim 146 words
In a process for the selective adsorption of one or more minor constituents from a bulk gas stream with a chabazite in which the bulk gas is size excluded from the pore structure of the chabazite or the minor constituted to be separated has a heat of adsorption greater than the bulk gas, the improvement which comprises separating the minor constituents utilizing a dehydrated calcium-exchanged chabazite having a Si/Al ratio of 1.9 to 2.3, a cation siting value f s , of about 0.9 to 1, a cation distribution value, f d , of about 0.74 to 1 and an adsorption capacity, C v , of at least about 40 cc N 2 /g at 30 ° C. and 1 atm under conditions such that the partial pressure of the minor constituent is in the linear low pressure region of the isotherm for the minor constituent.
Claim 3
Dependent Claim 26 words
The process of claim 1 wherein the minor constituent is nitrogen and the bulk gas is argon, hydrogen, helium, krypton, neon, xenon, tetrafluoromethane or mixtures thereof.
Claim 4
Dependent Claim 25 words
The process of claim 1 wherein the minor constituent is carbon monoxide, nitrogen, methane or mixtures thereof and the bulk gas is hydrogen or helium.
Claim 5
Dependent Claim 29 words
The process of claim 3 wherein the chabazite has an adsorptive capacity, C v , of 45 to 56 cc N 2 /g at 30° C. and 1 atm.
Claim 6
Dependent Claim 31 words
The process of claim 1 wherein the chabazite has a Si/Al ratio of 2, a cation siting, f s , of 1 and a cation distribution, f d , of 1.
Claim 7
Dependent Claim 27 words
The process of claim 5 wherein the chabazite has an adsorptive capacity, C v of about 56 cc N 2 /g at 30° C. and 1 atm.
Claim 8
Dependent Claim 25 words
The process of claim 1 wherein the chabazite has the composition Ca 2+ x/2 [(SiO 2 ) 12-x (AlO 2 ) x ] wherein x=3.64-4.14.

References Cited (Backward Citations)

GB841812A Cited
US4481018A Cited
US4544378A Cited
US4663052A Cited
US4713362A Cited
US4732584A Cited
US4747854A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-07-23 1994-01-22 1994-07-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-07-23 1998-01-22 1998-07-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-07-23 2002-01-22 2002-07-24 $7700.00 Window Closed / Lapsed

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