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US3679769A Expired / Lapsed US ⏱️ 0.0 years remaining

Alkyl transfer of alkyl aromatics with group viii metals on zeolites

Assignee: Ashland LLC
•
Filing: 1968-12-19
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Granted: 1972-07-25
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Expires: 1988-12-19
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Abstract

Abstract A process for the alkyl transfer of alkyl aromatics including contacting an alkyl aromatic feed material, such as toluene, with a catalyst comprising a precious metal of Group VIII, such as platinum, palladium, rhodium, ruthenium, etc., deposited on a zeolite base at a temperature of about 700* to 1,100* F, a pressure of about 0 to 2,000 psig, and a liquid hourly space velocity of about 0.1 to 10, and in the presence of hydrogen introduced at a rate of about 1 to 10 moles hydrogen per mole of hydrocarbon feed. Promoters selected from Group I, Group II, Group IV, and the Rare Earth metals of the Periodic System may be added to the catalyst. Deactivated catalyst may be periodically rejuvenated by discontinuing the introduction of aromatic feed material and purging with hydrogen and the catalyst can be reactivated by calcination in air. Where toluene is the feed, the alkyl transfer product may be distilled to separate benzene, toluene and xylenes, the toluene may be recycled to the alkyl transfer step, the xylenes may be crystallized to separate paraxylene from the remaining xylenes, the mother liquor from the crystallization step may thereafter be isomerized to readjust the para-xylene content and the product of the isomerization may be recycled to the crystallization zone.

Inventors

  • 👤 Ronald A Kmecak
  • 👤 Stephen M Kovach

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 19:55
CPC Classifications
C; C07; C07C; C07C15/00; C07C15/02; C07C15/067; C07C15/08; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/064; B01J29/068; C07C5/00; C07C5/22; C07C5/27; C07C5/2702; C07C5/2724; C07C6/00; C07C6/08; C07C6/12; C07C6/123; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52; Y02P20/584

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 34 words
A process in accordance with claim 1 wherein the flow of feed material through the catalyst is interrupted periodically and the flow of hydrogen is continued for a time sufficient to reactive the catalyst.
Claim 2
Dependent Claim 34 words
A process in accordance with claim 1 wherein the flow of feed material and hydrogen through the catalyst is discontinued and the catalyst is calcined in air under conditions sufficient to reactivate the catalyst.
Claim 3
Dependent Claim 16 words
A process in accordance with claim 1 wherein the feed material contains substantial volumes of toluene.
Claim 4
Dependent Claim 27 words
A process in accordance with claim 4 wherein unconverted toluene is separated from the alkyl transfer product and said unconverted toluene is recycled to the disproportionation step.
Claim 5
Dependent Claim 23 words
A process in accordance with claim 4 wherein xylenes are separated from the alkyl transfer product and para-xylene is separated from said xylenes.
Claim 6
Dependent Claim 72 words
A process in accordance with claim 6 wherein the xylenes remaining after the separation of para-xylene are subjected to isomerization, at a temperature of about 500* to 900* F., a pressure of about 50 to 2,000 psig., a liquid hourly space velocity of about 0.1 to 10 and in the presence of hydrogen at a mol ratio of about 1 to 20 mols hydrogen per mol of hydrocarbon, to produce additional paraxylene.
Claim 7
Dependent Claim 129 words
A process for the alkyl transfer of alkyl aromatics; comprising, contacting an alkyl aromatic feed material with a catalyst consisting essentially of about 0.01 to 1percent by weight of the finished catalyst of platinum and about 1 to 15percent by weight of a metal oxide of a metal selected from the group consisting of Group IV and the Rare Earth metals of the periodic system and mixtures thereof deposited on a synthetic zeolite base having a silicon-to-aluminum ratio below about 5 to 1, while maintaining a temperature of about 800* to 1,000* F., about 300 to 600 psig, a liquid hourly space velocity of about 0.1 to 10, and a hydrogen-to-hydrocarbon mol ratio of between about 1 and 10 to 1, to cause alkyl transfer of said alkyl aromatics.

References Cited (Backward Citations)

US2795629A Cited
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US3410921A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-07-25 1976-01-24 1976-07-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-07-25 1980-01-24 1980-07-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-07-25 1984-01-24 1984-07-25 $7700.00 Window Closed / Lapsed

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