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US4014949A
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Separation of cyclic compounds with molecular sieve adsorbent
Assignee: Sun Ventures Inc
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Filing: 1973-12-19
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Granted: 1977-03-29
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Expires: 1993-12-19
Abstract
Abstract Selective adsorption of one cyclic compound from a fluid mixture with a structurally similar cyclic compound can be obtained with molecular sieves (crystalline aluminosilicate zeolites) which have been partially dehydrated at a temperature in the range of 80°-300°C. Preferably the Al/Si ratio in the zeolite framework is in the range of 0.2-0.65. For example, m-xylene can be separated from p-xylene by selective adsorption of the m-xylene on NaY zeolite which was partially dehydrated at 125° C. and contains about 12 wt % water by ignition analysis.
Inventors
- 👤 John A. Hedge
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 08:43
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/12; C07C7/13; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/08; B01J29/084; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/08; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
158 words
A process for separating two structurally similar cyclic hydrocarbons selected from the group consisting of benzene, toluene and xylenes, said process comprising: A. contacting a fluid feed mixture comprising said cyclic hydrocarbons with a solid adsorbent comprising a partially dehydrated, substantially crystalline alumino-silicate sodium Y zeolite having a critical pore diameter greater than about 6A, the ratio Al/Si of the alumino-silicate framework of the zeolite being in the range of 0.65-0.2, the zeolite having been partially dehydrated to a water content of 6-20 weight percent exposure to a temperature in the range of 80°-300°C., whereby there is obtained a rich adsorbent containing an adsorbate which is richer in one said cyclic hydrocarbon than was said fluid feed mixture, and a raffinate product which contains less of the one said cyclic hydrocarbon than did said fluid feed mixture; B. separating said raffinate product from said rich adsorbent and, C. removing the one said cyclic hydrocarbon from said rich adsorbent.
Claim 2
Dependent Claim
158 words
A process for separating two structurally similar cyclic hydrocarbons selected from the group consisting of benzene, toluene and xylenes, said process comprising: A. contacting a fluid feed mixture comprising said cyclic hydrocarbons with a solid adsorbent comprising a partially dehydrated, substantially crystalline alumino-silicate sodium Y zeolite having a critical pore diameter greater than about 6A, the ratio Al/Si of the alumino-silicate framework of the zeolite being in the range of 0.65-0.2, the zeolite having been partially dehydrated to a water content of 6-20 weight percent exposure to a temperature in the range of 80°-300°C., whereby there is obtained a rich adsorbent containing an adsorbate which is richer in one said cyclic hydrocarbon than was said fluid feed mixture, and a raffinate product which contains less of the one said cyclic hydrocarbon than did said fluid feed mixture; B. separating said raffinate product from said rich adsorbent and, C. removing the one said cyclic hydrocarbon from said rich adsorbent.
Claim 3
Dependent Claim
47 words
Process according to claim 1 wherein said substantially crystalline alumino-silicate zeolite is at least 50% crystalline by X-ray, compared to a fully hydrated pure specimen of said zeolite, and wherein there is a loss of 8-18% weight percent water upon ignition analysis of said zeolite at 1900°F.
Claim 4
Dependent Claim
30 words
Process according to claim 1 wherein said loss of water upon ignition analysis is about 12 weight percent and wherein the said ratio Al/Si is in the range of 0.35-0.65.
Claim 5
Dependent Claim
17 words
Process according to claim 1 wherein p-xylene is separated from m-xylene by preferential adsorption of said p-xylene.
Claim 6
Dependent Claim
20 words
Process according to claim 1 wherein said zeolite has been partially dehydrated at a temperature in the range of 125°-175°C.
References Cited (Backward Citations)
US3126425A
Cited
US2988503A
Cited
US3130007A
Cited
US3485748A
Cited
BE734798A
Cited
US3558730A
Cited
US3626020A
Cited
US3665046A
Cited
US3668266A
Cited
US3699182A
Cited
US3668267A
Cited
US3840610A
Cited
US3663638A
Cited
US3686343A
Cited
US3734974A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-03-28 | 1980-09-27 | 1981-03-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-03-28 | 1984-09-27 | 1985-03-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-03-28 | 1988-09-27 | 1989-03-29 | $7700.00 | Window Closed / Lapsed |