US3720604A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Adsorbing olefins with a copper-exchanged type y zeolite
Assignee: Universal Oil Products Co
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Filing: 1971-08-16
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Granted: 1973-03-13
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Expires: 1991-08-16
Abstract
Abstract A new composition of matter, a method for the preparation of a copper-exchanged Type Y structured zeolite and a separation process employing the same. The zeolite adsorbent is prepared by a procedure employing an aqueous ion-exchange step and a final step including contacting the copper-exchanged zeolite with a mixture containing a cuprous salt and a hydrocarbon. The process involves the selective separation of olefinic hydrocarbons from saturated hydrocarbons employing a Type Y structured zeolite containing copper cations at the cationic exchange sites within the zeolite. The olefins are selectively retained by an adsorbent and are removed in a concentrated form by a desorption step.
Inventors
- 👤 D Rosback
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 20:56
CPC Classifications
C; C10; C10G; C10G25/00; C10G25/02; C10G25/03; B; B01; B01J; B01J20/00; B01J20/02; B01J20/10; B01J20/16; B01J20/18; B01J20/186; C07; C07C; C07C7/00; C07C7/12; C07C7/13
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
189 words
In a process for the separation of olefins from a feed mixture comprising olefins and saturated hydrocarbons which process comprises the steps of: a. contacting said feed mixture with a bed of a zeolite adsorbent at adsorption conditions to effect the selective retention of said olefins by said adsorbent; b. withdrawing from said bed of adsorbent a raffinate stream comprising less selectively retained saturated hydrocarbons; c. contacting the adsorbent bed with a Desorbent at desorption conditions to effect desorption of said olefins from said adsorbent; d. withdrawing a stream containing olefins and desorbent; wherein an improvement comprises employing a zeolite adsorbent prepared by the steps of: a. contacting a sodium form Type Y structured zeolite with an aqueous solution of a water-soluble copper salt at ion-exchange conditions to effect replacement of a portion of the sodium by copper cations; b. dehydrating at least a portion of said zeolite by heating dehydration conditions; and, c. contacting the zeolite with a mixture comprising a hydrocarbon and a cuprous salt, said hydrogen being capable of forming a soluble complex with the cuprous salt and passing within the pore openings of said zeolite.
Claim 2
Dependent Claim
189 words
In a process for the separation of olefins from a feed mixture comprising olefins and saturated hydrocarbons which process comprises the steps of: a. contacting said feed mixture with a bed of a zeolite adsorbent at adsorption conditions to effect the selective retention of said olefins by said adsorbent; b. withdrawing from said bed of adsorbent a raffinate stream comprising less selectively retained saturated hydrocarbons; c. contacting the adsorbent bed with a Desorbent at desorption conditions to effect desorption of said olefins from said adsorbent; d. withdrawing a stream containing olefins and desorbent; wherein an improvement comprises employing a zeolite adsorbent prepared by the steps of: a. contacting a sodium form Type Y structured zeolite with an aqueous solution of a water-soluble copper salt at ion-exchange conditions to effect replacement of a portion of the sodium by copper cations; b. dehydrating at least a portion of said zeolite by heating dehydration conditions; and, c. contacting the zeolite with a mixture comprising a hydrocarbon and a cuprous salt, said hydrogen being capable of forming a soluble complex with the cuprous salt and passing within the pore openings of said zeolite.
Claim 3
Dependent Claim
25 words
The process of claim 1 further characterized in that said hydrocarbon feed contains olefins having from about six to about 20 carbon atoms per molecule.
Claim 4
Dependent Claim
39 words
The process of claim 1 further characterized in that said adsorption and desorption conditions include temperatures within the range of from about 25*C. to about 175*C. and pressures within the range of from about atmospheric to about 500 psig.
Claim 5
Dependent Claim
19 words
The process of claim 3 further characterized in that said adsorption and desorption conditions are effected in liquid phase.
References Cited (Backward Citations)
US3510423A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1976-03-12 | 1976-09-11 | 1977-03-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1980-03-12 | 1980-09-11 | 1981-03-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1984-03-12 | 1984-09-11 | 1985-03-13 | $7700.00 | Window Closed / Lapsed |