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US4414406A Expired / Lapsed US ⏱️ 0.0 years remaining

Class of Friedel-crafts catalysts

Assignee: BP Corp North America Inc
•
Filing: 1981-09-18
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Granted: 1983-11-08
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Expires: 2001-09-18
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Abstract

Abstract Molybdenum compounds, particularly molybdenum sulfide, molybdenum silicide, molybdenum selenide and molybdenum telluride are useful Friedel-Crafts catalysts for the aralkylation of aromatics to produce polybenzyls, the manufacture of aromatic ketones, aromatic sulfones and aromatic esters. The foregoing processes are carried out at a temperature of about 60° to 250° C. and at a catalyst concentration of about 0.1 to 15% by weight of reactants. The reaction products are useful as laminates, herbicides and bactericides.

Inventors

  • 👤 Ellis K. Fields

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 21:59
CPC Classifications
C; C07; C07C; C07C317/00; B; B01; B01J; B01J27/00; B01J27/02; B01J27/04; B01J27/047; B01J27/051; B01J27/057; B01J27/0573; B01J27/0576; C07C37/00; C07C37/11; C07C37/18; C07C45/00; C07C45/45; C07C45/46; C07C49/00; C07C49/76; C07C49/782; C07C49/784; C08; C08F; C08F8/00; C08F8/02; C08G; C08G61/00; C08G61/02; C08G75/00; C08G75/20

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 79 words
A process for the production of polybenzyls by aralkylation of aromatic hydrocarbons which comprises contacting the same or different aromatic halides in the presence of a molybdenum contacting catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 , wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% weight of reactants.
Claim 2
Dependent Claim 79 words
A process for the production of polybenzyls by aralkylation of aromatic hydrocarbons which comprises contacting the same or different aromatic halides in the presence of a molybdenum contacting catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 , wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% weight of reactants.
Claim 3
Dependent Claim 11 words
The process of claim 1 wherein the reactant is benzyl chloride.
Claim 4
Dependent Claim 11 words
The process of claim 1 wherein the reactant is vinylbenzyl chloride.
Claim 5
Dependent Claim 11 words
The process of claim 1 wherein the reactant is benzyl chloroformate.
Claim 6
Dependent Claim 14 words
The process of claim 1 wherein the reactants are benzyl chloride and a,a' dichloro-p-xylene.
Claim 7
Dependent Claim 74 words
A process for the production of substituted benzophenones which process comprises contacting aroyl halides with aromatic hydrocarbons in the presence of a molybdenum containing catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% weight of reactants.
Claim 8
Dependent Claim 74 words
A process for the production of substituted benzophenones which process comprises contacting aroyl halides with aromatic hydrocarbons in the presence of a molybdenum containing catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% weight of reactants.
Claim 9
Dependent Claim 20 words
The process of claim 6 wherein the reactants are m-toluoyl chloride and p-xylene and wherein the product is 2,4,3' trimethylbenzophenone.
Claim 10
Dependent Claim 75 words
A process for the production of aromatic hydrocarbon sulfones, which comprises contacting arylsulfonyl halides with aromatic hydrocarbons in the presence of a molybdenum containing catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% by weight of reactants.
Claim 11
Dependent Claim 75 words
A process for the production of aromatic hydrocarbon sulfones, which comprises contacting arylsulfonyl halides with aromatic hydrocarbons in the presence of a molybdenum containing catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% by weight of reactants.
Claim 12
Dependent Claim 22 words
The process of claim 8 wherein the reactants are p-xylene and p-toluene sulfonyl chloride and the product is 2,5,4' trimethyl diphenyl sulfone.
Claim 13
Dependent Claim 72 words
A process for the benzylation of polystyrene which comprises contacting benzyl halide with polystyrene in the presence of a molybdenum containing catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% by weight of reactants.
Claim 14
Dependent Claim 72 words
A process for the benzylation of polystyrene which comprises contacting benzyl halide with polystyrene in the presence of a molybdenum containing catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% by weight of reactants.
Claim 15
Dependent Claim 15 words
A process for the benzylation of phenols which comprises contacting phenols with halogenated aromatic hydrocarbons.
Claim 16
Dependent Claim 15 words
A process for the benzylation of phenols which comprises contacting phenols with halogenated aromatic hydrocarbons.
Claim 17
Dependent Claim 52 words
The process of claim 11 wherein the reactants are phenol and benzyl chloride and the product is benzyl phenol and wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% by weight of reactants.
Claim 18
Dependent Claim 73 words
A process for production of aromatic hydrocarbon esters which comprises contacting aroyl halides and phenols in the presence of a molybdenum containing catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% by weight of reactants.
Claim 19
Dependent Claim 73 words
A process for production of aromatic hydrocarbon esters which comprises contacting aroyl halides and phenols in the presence of a molybdenum containing catalyst selected from the group consisting of MoS 2 , MoSi 2 , MoTe 2 , and MoSe 2 wherein the reaction is conducted at a temperature of about 60° to 250° C. and the catalyst concentration is in the range of about 0.01 to about 15% by weight of reactants.
Claim 20
Dependent Claim 19 words
The process of claim 13 wherein the reactants are benzyl chloride and phenol and the ester is phenyl benzoate.

References Cited (Backward Citations)

US3329826A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-11-07 1987-05-09 1987-11-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-11-07 1991-05-09 1991-11-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-11-07 1995-05-09 1995-11-08 $7700.00 Window Closed / Lapsed

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