Shell Oil Comapny

Pieter A Gautier

Arien Kwantes

Eit Drent

Johannes A Van Broekhoven

Johannes J Keijsper

Leonardus Petrus

Rudolf Jacobus Wijngaarden

Wiebren Age Miedema

Maarten M Geuze

Barend Mastenbroek

Anthony L Farragher

An improved, continuous, gas-phase process for the production of linear alternating polymers of carbon monoxide and at least one ethylenically unsaturated hydrocarbon in the presence of a supported catalyst composition, the catalyst composition being formed from a compound of palladium, a Lewis acid and a bidentate ligand of phosphorus, includes return to the polymerization reactor of relatively small particles of polyketone polymer products after catalyst composition has been supplied to the particles.

Continuous gas phase polymerization of CO/olefin with palladium and

An improved process for the production of linear alternating polymers of carbon monoxide and at least one ethylenically unsaturated hydrocarbon comprises contacting the carbon monoxide and ethylenically unsaturated hydrocarbon under polymerization conditions in inert reaction diluent in the presence of a catalyst composition formed from a compound of palladium, a bidentate ligand of phosphorus, sulfur or nitrogen and an alkyl ester or anhydride of a monocarboxylic or dicarboxylic acid.

Polymerization of olefin/carbon monoxide with palladium salt, bidentate

An improved process for the production of linear alternating polymers of carbon monoxide and at least one ethylenically unsaturated hydrocarbon by contacting the carbon monoxide and hydrocarbon under polymerization conditions in the presence of a catalyst composition formed from a palladium compound, a strong non-hydrohalogenic acid and a bidentate ligand of phosphorus, nitrogen or sulfur comprises conducting the polymerization in a continuous manner in two or more reactors connected in series.

Continuous polymerization of Co/olefin in plurality of reactors in series

A process for the preparation of bisphenols is described which comprises reacting, in a reaction zone, at least 2 moles of a phenol with a carbonyl compound, at a temperature of from 40.degree. to 95.degree. C., in the presence of an acid ion exchanger, optionally partially modified with a compound having an acidic reacting group and a mercaptan group, and recovering the bisphenols from the reaction zone effluent, characterized in that the reaction zone effluent is contacted with an acid ion exchanger in metal salt form and/or a weak base ion exchanger. As a result, it has been found that the formation of undesirable compounds is substantially reduced.

Preparation of bisphenols

An improved process for preparing bisphenols is described wherein a phenol is reacted with a ketone or aldehyde such as acetone in the presence of an ion-exchange resin modified by partial neutralization with p-aminothiophenol.

Growing community of inventors

Amsterdam, Netherlands

Pieter A Gautier