Patent US4014949A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4014949A Expired / Lapsed US ⏱️ 0.0 years remaining

Separation of cyclic compounds with molecular sieve adsorbent

Assignee: Sun Ventures Inc
•
Filing: 1973-12-19
•
Granted: 1977-03-29
•
Expires: 1993-12-19
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

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.

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

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag