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US3969223A Expired / Lapsed US ⏱️ 0.0 years remaining

Olefin separation process

Assignee: Universal Oil Products Co
•
Filing: 1974-12-11
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Granted: 1976-07-13
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Expires: 1994-12-11
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Abstract

Abstract An improved process for the separation of olefins from a hydrocarbon feed mixture comprising olefins and saturates which process uses a zeolite adsorbent to selectively adsorb the olefins. The improvement comprises employing a zeolite adsorbent produced by the steps of: contacting a precursor mass containing type X structured zeolite and amorphous material as a binder with an aqueous caustic solution to effect the addition of alkali metal cations to the crystalline structure; washing the mass with water to remove therefrom excess caustic solution; and, at least partially dehydrating said mass at dehydrating conditions thereby producing an adsorbent which has both increased capacity for olefins and decreased catalytic activity.

Inventors

  • 👤 Donald H. Rosback
  • 👤 Richard W. Neuzil

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 07:11
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: 7
Claim 1
Independent Claim 250 words
In a process for the separation of olefins from a hydrocarbon feed mixture comprising olefins from a hydrocarbon feed mixture comprising olefins and saturates, which process comprises the steps of: a. contacting said feed mixture with a bed of zeolite adsorbent at adsorption conditions to effect the selective adsorption of said olefins by said adsorbent; b. withdrawing from said bed of adsorbent a raffinate stream comprising less selectively adsorbed saturates; c. contacting the adsorbent bed with a desorbent material at desorption conditions to effect desorption of said olefins from said adsorbent; and, d. withdrawing a stream containing olefins and desorbent material from said bed of adsorbent; THE IMPROVEMENT WHICH COMPRISES employing a zeolite adsorbent prepared by the steps of: i. contacting a precursor mass comprising an X structured zeolite, and an amorphous binder selected from the group consisting of silica, alumina, and silica-alumina, and having a Na 2 O/Al 2 O 3 ratio of less than about 0.7 with an aqueous sodium hydroxide solution at ion exchange conditions for 0.5 to 5 hours to increase the sodium cation content to a Na 2 O/Al 2 O 3 ratio of greater than about 0.7 and to remove from about 1 to about 15 wt. % of SiO 2 and Al 2 O 3 from the precursor mass; ii. washing said mass with water maintained at a pH within the range of 7 to 10 to remove therefrom excess sodium hydroxide; and, iii. at least partially dehydrating said meass at dehydrating conditions.
Claim 2
Dependent Claim 250 words
In a process for the separation of olefins from a hydrocarbon feed mixture comprising olefins from a hydrocarbon feed mixture comprising olefins and saturates, which process comprises the steps of: a. contacting said feed mixture with a bed of zeolite adsorbent at adsorption conditions to effect the selective adsorption of said olefins by said adsorbent; b. withdrawing from said bed of adsorbent a raffinate stream comprising less selectively adsorbed saturates; c. contacting the adsorbent bed with a desorbent material at desorption conditions to effect desorption of said olefins from said adsorbent; and, d. withdrawing a stream containing olefins and desorbent material from said bed of adsorbent; THE IMPROVEMENT WHICH COMPRISES employing a zeolite adsorbent prepared by the steps of: i. contacting a precursor mass comprising an X structured zeolite, and an amorphous binder selected from the group consisting of silica, alumina, and silica-alumina, and having a Na 2 O/Al 2 O 3 ratio of less than about 0.7 with an aqueous sodium hydroxide solution at ion exchange conditions for 0.5 to 5 hours to increase the sodium cation content to a Na 2 O/Al 2 O 3 ratio of greater than about 0.7 and to remove from about 1 to about 15 wt. % of SiO 2 and Al 2 O 3 from the precursor mass; ii. washing said mass with water maintained at a pH within the range of 7 to 10 to remove therefrom excess sodium hydroxide; and, iii. at least partially dehydrating said meass at dehydrating conditions.
Claim 3
Dependent Claim 26 words
The process of claim 1 further characterized in that said hydrocarbon feed mixture contains olefins having from about 4 to about 20 carbon atoms per molecule.
Claim 4
Dependent Claim 40 words
The process of claim 1 further characterized in that said adsorption and desorption conditions include temperatures within the range of from about 25° to about 150° C. and pressures within the range of from about atmospheric to about 500 psig.
Claim 5
Dependent Claim 20 words
The process of claim 1 further characterized in that said adsorption and desorption conditions are effected in the liquid phase.
Claim 6
Dependent Claim 25 words
The process of claim 1 further characterized in that said desorbent material has an average boiling range substantially different than that of the feed mixture.
Claim 7
Dependent Claim 17 words
The process of claim 5 further characterized in that said desorbent material comprises a straight chain olefin.

References Cited (Backward Citations)

US3265750A Cited
US3326797A Cited
US3717572A Cited
US3706813A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-07-13 1980-01-12 1980-07-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-07-13 1984-01-12 1984-07-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-07-13 1988-01-12 1988-07-13 $7700.00 Window Closed / Lapsed

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