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US3720604A Expired / Lapsed US ⏱️ 0.0 years remaining

Adsorbing olefins with a copper-exchanged type y zeolite

Assignee: Universal Oil Products Co
•
Filing: 1971-08-16
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Granted: 1973-03-13
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Expires: 1991-08-16
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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

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