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US4220604A Expired / Lapsed US ⏱️ 0.0 years remaining

Oxidative rearrangement of olefins

Assignee: Phillips Petroleum Co
•
Filing: 1978-07-14
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Granted: 1980-09-02
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Expires: 1998-07-14
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Abstract

Abstract An isoolefin is converted to a ketone, e.g., isobutylene to methyl ethyl ketone, by an oxidative rearrangement in a two-phase diluent system in the presence of free oxygen, a suitable surfactant, and a catalyst system comprising palladium, copper, and an alkali or alkaline earth metal chloride.

Inventors

  • 👤 Paul R. Stapp

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 19:13
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/27; C07C45/32; C07C45/33; C07C45/34; C07C45/35; C07C29/00; C07C29/48; C07C29/50

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 305 words
A process for the conversion of an isoolefin reactant to a ketone which comprises contacting: (a) an isoolefin which has the general formula: ##STR5## wherein R 1 and R 2 are alkyl radicals containing from 1 to about 8 carbon atoms per radical with (b) oxygen in (c) a reaction diluent comprising at least two liquid phases wherein at least one liquid phase is an aqueous phase, in the presence of (d) a catalyst comprising palladium, copper, and an alkali metal or alkaline earth metal chloride, and (e) a surfactant, wherein said surfactant is selected from the group consisting of: (1) quaternary ammonium salts of the general formula (R'").sub.4 N.sup.+ X.sup.-, (2) alkali metal alkyl sulfates of the general formula R' v OSO 3 M, (3) alkali metal salts of alkanoic acids of the general formula R' v CO 2 M, (4) alkali metal salts of alkaryl sulfonic acids of the general formula ##STR6## (5) 1-alkyl pyridinium salts of the general formula ##STR7## wherein R'" is an alkyl radical of from 1 to 20 carbon atoms and wherein the total number of carbon atoms in said quaternary ammonium salt is from about 8 to about 30 carbon atoms; X - is selected from the group consisting of Br - , Cl - , I - , F - , R'"CO 2 - , QSO 3 - , BF 4 - , HSO 4 - wherein Q is an aryl or alkaryl radical of 6 to 10 carbon atoms; R' v is an alkyl radical of from 10 to about 20 carbon atoms; M is an alkali metal; R v is an alkyl radical of 1 to 4 carbon atoms and wherein n is 0 or an integer of from 1 to 4, under such reaction conditions that the isoolefin undergoes oxidative rearrangement to a ketone.
Claim 2
Dependent Claim 305 words
A process for the conversion of an isoolefin reactant to a ketone which comprises contacting: (a) an isoolefin which has the general formula: ##STR5## wherein R 1 and R 2 are alkyl radicals containing from 1 to about 8 carbon atoms per radical with (b) oxygen in (c) a reaction diluent comprising at least two liquid phases wherein at least one liquid phase is an aqueous phase, in the presence of (d) a catalyst comprising palladium, copper, and an alkali metal or alkaline earth metal chloride, and (e) a surfactant, wherein said surfactant is selected from the group consisting of: (1) quaternary ammonium salts of the general formula (R'").sub.4 N.sup.+ X.sup.-, (2) alkali metal alkyl sulfates of the general formula R' v OSO 3 M, (3) alkali metal salts of alkanoic acids of the general formula R' v CO 2 M, (4) alkali metal salts of alkaryl sulfonic acids of the general formula ##STR6## (5) 1-alkyl pyridinium salts of the general formula ##STR7## wherein R'" is an alkyl radical of from 1 to 20 carbon atoms and wherein the total number of carbon atoms in said quaternary ammonium salt is from about 8 to about 30 carbon atoms; X - is selected from the group consisting of Br - , Cl - , I - , F - , R'"CO 2 - , QSO 3 - , BF 4 - , HSO 4 - wherein Q is an aryl or alkaryl radical of 6 to 10 carbon atoms; R' v is an alkyl radical of from 10 to about 20 carbon atoms; M is an alkali metal; R v is an alkyl radical of 1 to 4 carbon atoms and wherein n is 0 or an integer of from 1 to 4, under such reaction conditions that the isoolefin undergoes oxidative rearrangement to a ketone.
Claim 3
Dependent Claim 24 words
The process of claim 1 wherein R 1 and R 2 are alkyl radicals containing from 1 to about 3 carbon atoms per radical.
Claim 4
Dependent Claim 117 words
The process of claim 1 wherein: the molar ratio of copper to palladium is about 1:1 to about 200:1; the molar ratio of the chloride ion derived from the alkali metal or alkaline earth metal chloride to palladium is about 2:1 to about 1,000:1; the molar ratio of the isoolefinic reactant to palladium is about 5:1 to about 1,000:1; the molar ratio of said surfactant to palladium is about 0.01:1 to about 10:1; the pressure of oxygen in the reaction system is in the range of from about 2 to about 250 psig above the autogenous pressure at the temperature utilized; and said reaction temperature is in the range of about 20° C. to about 200° C.
Claim 5
Dependent Claim 45 words
The process of claim 1 wherein the diluent consists of two phases, one aqueous and the other an organic phase wherein said organic phase is relatively inert to the oxidation conditions employed, inert to hydrolysis-type reactions, and shows a limited solubility in the aqueous phase.
Claim 6
Dependent Claim 55 words
The process of claim 4 wherein the amount of organic diluent is in the range of about 50 to about 1000 ml of organic diluent per mole of isoolefinic reactant and the amount of aqueous phase is in the range of about 50 to about 1000 ml of aqueous phase per mole of isoolefinic reactant.
Claim 7
Dependent Claim 19 words
The process of claim 1 wherein said isoolefinic reactant is isobutylene and the ketone formed is methyl ethyl ketone.
Claim 8
Dependent Claim 39 words
The process of claim 6 wherein: the reaction diluent is an aqueous phase and an organic phase with the organic phase being chlorobenzene; the catalyst is palladium chloride, cupric chloride, and lithium chloride; and the surfactant is hexadecyltrimethylammonium bromide.
Claim 9
Dependent Claim 35 words
The process of claim 6 wherein t-butyl alcohol is also a reaction product with said t-butyl alcohol being subjected to dehydration in order to form isobutylene which is then recycled to the oxidation reaction zone.

References Cited (Backward Citations)

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US3365499A Cited
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US3992432A Cited
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USPTO Annuity & Maintenance Windows

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