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US3697606A Expired / Lapsed US ⏱️ 0.0 years remaining

Para-phenylphenol preparation

Assignee: Union Carbide Corp
•
Filing: 1968-03-20
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Granted: 1972-10-10
•
Expires: 1988-03-20
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Abstract

Abstract The process of preparing para-phenylphenol by heating parahexenylphenol in the liquid phase in the presence of a stoichiometric excess of a hydrogen acceptor, and a palladium, nickel or platinum catalyst.

Inventors

  • 👤 Joachim E Freudewald
  • 👤 Frederic M Konrad

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 14:29
CPC Classifications
C; C07; C07C; C07C37/00; C07C37/06; C07C37/11; C07C37/20; C07C37/50; C07C37/52; C07C2601/00; C07C2601/12; C07C2601/14

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 175 words
The process of preparing para-phenylphenol by the steps comprising: a. condensing about two moles of phenol with about one mole of cyclohexanone in the presence of a strong acid condensation catalyst at a temperatuRe of from about 40* C to about 120* C to form 1,1-bis(p-hydroxyphenol)cyclohexane; b. cleaving the formed 1,1-bis(p-hydroxylphenyl)-cyclohexane in the presence of an acidic or basic cleavage catalyst at a temperature of from about 150* C to about 250* C to form para-cyclohexenylphenol; and c. dehydrogenating the formed para-cyclohexenylphenol in an exothermic hydrogen transfer reaction by heating the reaction product of step (b) to a temperature of from about 100* C to about 180* C in the liquid phase with a stoichiometric excess of a hydrogen acceptor which is selected from the group consisting of ethylenically unsaturated hydrocarbons, acetylenically unsaturated hydrocarbons, azobenzene, Alpha -methylstyrene, nitrobenzene, para-nitrophenol, para-chloronitrobenzene, maleic anhydride, diketone methyl acetylene, indene, crotonic acid and sorbic acid; and a catalyst selected from the group consisting of nickel, palladium, platinum, rhodium, ruthenium, platinum oxide, platinum black, cobalt, nickel sulfide, iron and molybdenum.
Claim 2
Dependent Claim 17 words
The process of claim 2 wherein the condensation catalyst is hydrochloric acid and a lower alkyl mercaptan.
Claim 3
Dependent Claim 13 words
The process of claim 2 wherein the cleavage catalyst is a basic catalyst.
Claim 4
Dependent Claim 13 words
The method of claim 2 wherein the cleavage catalyst is an alkali hydroxide.
Claim 5
Dependent Claim 13 words
The method of claim 2 wherein the cleavage catalyst is a weak acid.
Claim 6
Dependent Claim 12 words
The method of claim 2 wherein the cleavage catalyst is sodium hydroxide.
Claim 7
Dependent Claim 12 words
The process of claim 1 wherein the hydrogen acceptor is Alpha -methylstyrene.
Claim 8
Dependent Claim 11 words
The process of claim 1 wherein the hydrogen acceptor is p-nitrophenol.

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) 1975-10-10 1976-04-10 1976-10-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-10-10 1980-04-10 1980-10-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-10-10 1984-04-10 1984-10-10 $7700.00 Window Closed / Lapsed

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