Shell Oil Comapny

Johan G Bitter

Johannes L Den Boestert

Johannes P Haan

Richard Hugh Clark

Jacobus Hendrikus Scheerman

Rudolf J Maas

Jayantilal B Rajani

Hendrik C Rijkens

Harry Futselaar

Wilhelmus J Weeres

Imre G Racz

A counter-current flow membrane module for liquid separations consisting of a body comprising hollow fiber membranes wherein the hollow fiber membranes are arranged transversely of the longitudinal axis of the module and the channels in the hollow fibers are connected to spaces present around the body which is furthermore surrounded by a shell. The module comprises two or more transverse current flow (cross-flow) segments formed by seals between the body and the shell, wherein at least one fiber layer or fiber fabric is applied per segment.

Counter-current membrane module for liquid separation

Process for reducing the metal content of a hydrocarbon feed mixture by reverse osmosis, comprising contacting the feed mixture substantially boiling in the range between about 100.degree. and about 350.degree. C. and containing at most about 1000 parts per billion by weight (ppbw) of metal(s) with a metal-selective membrane to give a hydrocarbon permeate stream having a metal content which is less.

Process for reducing the metal content of a hydrocarbon mixture

The invention relates to a process for the separation of a phenol from a mixture obtained by the carboxylation of the phenol and containing phenol, phenolate and the carboxylation products thereof, which process comprises separation carried out by selectively absorbing the phenol into the wall of a membrane, solubilizing the phenol in the membrane matrix, diffusing the phenol through the membrane and desorbing the phenol from the other wall.

Process for the separation of a phenol

A supported membrane comprising a non-woven monofilament support layer wherein dense membranes with a maximum width of 5000 .mu.m are surrounded by filaments. The invention further relates to a process for the preparation of said supported membranes.

Supported membrane and process for its preparation

Process for separating a fluid feed mixture containing hydrocarbon oil and an organic solvent (e.g. obtained from a furfural extraction unit) by contacting said fluid feed mixture at elevated pressure with one side of a hydrocarbon oil-selective membrane containing a layer of a silicone polymer which is substantially impermeable to said organic solvent and recovering hydrocarbon oil permeate from the other side of the membrane.

Process for separating a fluid feed mixture containing hydrocarbon oil

A supported membrane comprising a non-woven monofiliment support layer wherein dense membranes with a maximum width of 5000 .mu.m are surrounded by filaments. The invention further relates to a process for the preparation of said supported membranes.

Supported membrane

The invention is a process for the separation of solvents from hydrocarbons dissolved in the solvents which comprises contacting at elevated pressure a feed solution comprising hydrocarbons dissolved in an aromatic solvent and a polar aliphatic solvent with one side of a dense membrane which is substantially impermeable to the hydrocarbons, and which membrane comprises a layer of a halogen-substituted silicon compound, and recovering the solvents from the other side of the membrane.

Process for the separation of solvents from hydrocarbons dissolved in

A process for the separation of a two component liquid mixture is described in which the liquid mixture is passed along one side of a membrane and an extracting agent is passed on the other side of the membrane, the process being characterized by the use of a membrane impermeable to at least one component of the liquid mixture and permeable to the extracting agent.

Process for the separation of an organic liquid mixture

An improved process is described for the preparation of 2,3,5-trimethylhydroquinone by catalytically oxidizing a trimethylphenol selected from the class consisting of 2,3,5-trimethylphenol, 2,3,6-trimethylphenol and mixtures thereof with oxygen in the presence of a cobalt chelate catalyst complex in a dimethylformamide solvent to form 2,3,5-trimethyl-p-benzoquinone which is subsequently hydrogenated to 2,3,5-trimethylhydroquinone by reaction with hydrogen in the presence of a noble metal catalyst. In this improved process, the 2,3,5-trimethyl-p-benzoquinone-containing reaction mixture from catalytic oxidation is contacted with di-n-butyl ether and water to form a di-n-butyl ether phase containing the 2,3,5-trimethyl-p-benzoquinone, a precipitate comprising the cobalt catalyst and an aqueous phase containing the dimethylformamide solvent, said di-n-butyl ether phase being subsequently separated from the precipitate and aqueous phase and passed to the catalytic hydrogenation reaction where the di-n-butyl ether functions as the reaction solvent.

Growing community of inventors

Amsterdam, Netherlands

Johan G Bitter