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US3607961A Expired / Lapsed US ⏱️ 0.0 years remaining

Alkyl transfer of alkyl aromatics with group viii metals on boria-alumina

Assignee: Ashland LLC
•
Filing: 1968-12-19
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Granted: 1971-09-21
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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 Group VIII metal, such as nickel, platinum, or palladium and boria deposited on an alumina base at a temperature of about 800* to 1100* F., a pressure of about 0 to 2000 p.s.i.g., 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 an atmosphere such as 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 para-xylene 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

  • 👤 Stephen M Kovach
  • 👤 Ronald A Kmecak

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 16:40
CPC Classifications
C; C07; C07C; C07C15/00; C07C15/02; C07C15/067; C07C15/08; C07C5/00; C07C5/22; C07C5/27; C07C5/2702; C07C5/2724; C07C6/00; C07C6/08; C07C6/12; C07C6/123

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 23 words
A process in accordance with claim 1 wherein the Group VIII metal is a metal of the first transition series of Group VIII.
Claim 2
Dependent Claim 12 words
A process in accordance with claim 1 wherein the metal is nickel.
Claim 3
Dependent Claim 16 words
A process in accordance with claim 1 wherein the Group VIII metal is a precious metal.
Claim 4
Dependent Claim 16 words
A process in accordance with claim 1 wherein the feed material contains substantial volumes of toluene.
Claim 5
Dependent Claim 27 words
A process in accordance with claim 5 wherein unconverted toluene is separated from the alkyl transfer product and said unconverted toluene is recycled to the disproportionation step.
Claim 6
Dependent Claim 23 words
A process in accordance with claim 5 wherein xylenes are separated from the alkyl transfer product and paraxylene is separated from said xylenes.
Claim 7
Dependent Claim 26 words
A process in accordance with claim 7 wherein the xylenes remaining after the separation of paraxylene are subjected to isomerizaton conditions sufficient to produce additional paraxylene.
Claim 8
Dependent 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 reactivate the catalyst.
Claim 9
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 10
Dependent Claim 107 words
A process for the alkyl transfer of alkyl aromatics; comprising, contacting an alkyl aromatic feed with a catalyst comprising about 0.01 to 5 percent by weight of a metal of the first transition series of Group VIII of the Periodic System and about 5 to 25 percent by weight of boria deposited on an alumina base, under conditions sufficient to cause alkyl transfer of said alkyl aromatics including a temperature of about 800 to 1100* F., a pressure of about 0 to 2000 p.s.i.g. a liquid hourly space velocity of about 0.1 to 10, and hydrogen to hydrocarbon mol ratio between about 1 and 10 to 1.
Claim 11
Dependent Claim 16 words
A process in accordance with claim 11 wherein the feed material contains substantial volumes of toluene.
Claim 12
Dependent Claim 16 words
A process in accordance with claim 12 wherein unconverted toluene is recycled to the disproportionation step,
Claim 13
Dependent Claim 23 words
A process in accordance with claim 12 wherein xylenes are separated from the alkyl transfer product and paraxylene is separated from said xylenes.
Claim 14
Dependent Claim 26 words
A process in accordance with claim 14 wherein the xylenes remaining after the separation of paraxylene are subjected to isomerization conditions sufficient to produce additional paraxylene.
Claim 15
Dependent Claim 34 words
A process in accordance with claim 11 wherein the flow of feed material through the catalyst is interrupted periodically and the flow of hydrogen is continued for a time sufficient to reactivate the catalysts.
Claim 16
Dependent Claim 34 words
A process in accordance with claim 11 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.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1974-09-20 1975-03-22 1975-09-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1978-09-20 1979-03-22 1979-09-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1982-09-20 1983-03-22 1983-09-21 $7700.00 Window Closed / Lapsed

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