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US4092371A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for manufacturing a catalyst comprising aluminum oxide and boron oxide, the resulting catalyst and the use thereof in alkylation reactions

Assignee: IFP Energies nouvelles
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Filing: 1977-07-07
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Granted: 1978-05-30
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Expires: 1997-07-07
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Abstract

Abstract A catalyst useful for the alkylation of aromatic hydrocarbons is produced by reacting a compound of the formula AlX y R.sub.(3 - y), where X is halogen, R is a hydrocarbon radical and y is 1, 3/2, 2 or 3, except 3 when X is fluorine, with a carrier comprising aluminum oxide and boron oxide.

Inventors

  • 👤 Jean-Pierre Franck
  • 👤 Jean-Francois Le Page

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 17:58
CPC Classifications
C; C07; C07C; C07C2/00; C07C2/54; C07C2/64; C07C2/66; C07C2/68; B; B01; B01J; B01J27/00; B01J27/06; B01J27/08; B01J37/00; B01J37/22; C07C2521/00; C07C2521/02; C07C2521/04; C07C2527/00; C07C2527/06; C07C2527/125; C07C2527/126; C07C2531/00; C07C2531/02; C07C2531/12; C07C2531/14; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/582

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 142 words
In the alkylation of an aromatic hydrocarbon with an olefin at about 100-300° C. and under sufficient pressure to maintain the aromatic hydrocarbon in the liquid phase and wherein the proportion of the olefin to the aromatic hydrocarbon is about 0.1 : 1 to 1 : 1, in contact with a catalyst, the improvement wherein said catalyst is that catalyst produced by reacting an aluminum compound of the formula AlX y R(3-y) where X is halogen, R is a hydrocarbon radical and y is 1, 3/2, or 2, with a carrier consisting essentially of a mixture of aluminum oxide and boron oxide in proportions by weight of 1 : 0.01 to 1 : 1, respectively, and wherein the compound of formula AlX y R.sub.(3-y) is used in a sufficient amount to introduce 0.5 - 20% by weight of halogen into the catalyst.
Claim 2
Dependent Claim 142 words
In the alkylation of an aromatic hydrocarbon with an olefin at about 100-300° C. and under sufficient pressure to maintain the aromatic hydrocarbon in the liquid phase and wherein the proportion of the olefin to the aromatic hydrocarbon is about 0.1 : 1 to 1 : 1, in contact with a catalyst, the improvement wherein said catalyst is that catalyst produced by reacting an aluminum compound of the formula AlX y R(3-y) where X is halogen, R is a hydrocarbon radical and y is 1, 3/2, or 2, with a carrier consisting essentially of a mixture of aluminum oxide and boron oxide in proportions by weight of 1 : 0.01 to 1 : 1, respectively, and wherein the compound of formula AlX y R.sub.(3-y) is used in a sufficient amount to introduce 0.5 - 20% by weight of halogen into the catalyst.
Claim 3
Dependent Claim 18 words
An alkylation process according to claim 1, wherein prior to use, the catalyst is heated to 300°-800° C.
Claim 4
Dependent Claim 40 words
An alkylation process according to claim 1, wherein the mixture of aluminum oxide and boron oxide for producing the catalyst results from impregnating alumina with an aqueous solution of boric acid, and the resultant mixture is heated to 100°-500° C.
Claim 5
Dependent Claim 23 words
An alkylation process according to claim 1, wherein the aluminum oxide has a specific surface of at least 5 square meters per gram.
Claim 6
Dependent Claim 31 words
An alkylation process according to claim 1, wherein a halogenated promoter is present in an amount of 10 to 10,000 ppm b.w. with respect to the aromatic hydrocarbon to be alkylated.
Claim 7
Dependent Claim 13 words
An alkylation process according to claim 1, wherein benzene is alkylated with ethylene.
Claim 8
Dependent Claim 22 words
An alkylation process according to claim 1, wherein benzene is alkylated with a mixture of hydrocarbons having 11 to 13 carbons atoms.
Claim 9
Dependent Claim 38 words
An alkylation process according to claim 1, wherein X is chlorine in the compound of the formula AlX y R.sub.(3-y), and said compound is used in a sufficient amount to introduce 4-12% b.w. of chlorine into the catalyst.
Claim 10
Dependent Claim 21 words
An alkylation process according to claim 1, wherein said reacting is carried out at a temperature of -20° to +250° C.
Claim 11
Dependent Claim 18 words
An alkylation process according to claim 2, wherein said heating is carried out at 400° - 600° C.
Claim 12
Dependent Claim 34 words
An alkylation process according to claim 1, wherein the catalyst is present in fixed bed and the feed rate is 0.25 to 20 volumes of liquid aromatic hydrocarbon per volume of catalyst per hour.

References Cited (Backward Citations)

US2480254A Cited
US2946778A Cited
US3054836A Cited
US3079328A Cited
US3096385A Cited
US3230270A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-05-29 1981-11-28 1982-05-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-05-29 1985-11-28 1986-05-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-05-29 1989-11-28 1990-05-30 $7700.00 Window Closed / Lapsed

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