Dupont Canada Inc.

Du Pont of Canada Limited

John R Boocock

Peter Y Kelly

David A Harbourne

Trevor C Arthurs

Ronald E Murray

Wayne F Bryce

Vaclav G Zboril

Richard W Oughton

Albert Bell

An adhesive composition formed by admixing under melt conditions (a) 50-95% by weight of a moisture cross-linkable silane-grafted polyolefin having a melt viscosity of less than 100,000 cps, and (b) 5-50% by weight of a polyolefin grafted with at least one ethylenically-unsaturated carboxylic acid or anhydride, and derivatives thereof. The grafted polyolefin has a melt viscosity of less than 100,000 cps, and contains a catalyst for moisture cross-linking of the silane-grafted polyolefin of (a). The adhesive may be used to bond a variety of substrates.

Cross-linkable adhesive polymers

An adhesive composition formed by admixing under melt conditions (a) 50-95% by weight of a moisture cross-linkable silane-grafted polyolefin having a melt viscosity of less than 100 000 cps, and (b) 5-50% by weight of a polyolefin grafted with at least one ethylenically-unsaturated carboxylic acid or anhydride, and derivatives thereof. The grafted polyolefin has a melt viscosity of less than 100 000 cps, and contains a catalyst for moisture cross-linking of the silane-grafted polyolefin of (a). The adhesive may be used to bond a variety of substrates.

A concentrate comprising a carrier polymer and at least 30%, by weight of the carrier polymer, of at least one modifying agent for a thermoplastic polymer is disclosed. The carrier polymer is a polymer of alpha-olefins having a heat of crystallization of less than 70 J/g and, if the copolymer is an ethylene/vinyl acetate copolymer, containing at least 18% by weight of vinyl acetate comonomer. The modifying agent is absorbed into the carrier polymer. In embodiments, the modifying agent is a polymerizable monomer. The concentrates provide a versatile method of addition of modifying agents into thermoplastic polymers.

Concentrates of modifying agents in polymers

A concentrate comprising a copolymer and 65 to 300%, by weight of the copolymer, of a vinyl silane is disclosed. The vinyl silane is vinyl trimethoxysilane and/or vinyl triethoxysilane. The copolymer is a copolymer of ethylene with at least one comonomer selected from the group consisting of carbon monoxide, vinyl acetate, alkyl acrylates and alkyl methacrylates, in which the alkyl groups have 1-4 carbon atoms. The copolymer is in a particulate form and has a heat of crystallization of less than 70 J/g, and if said copolymer is ethylene/vinyl acetate copolymer, then the copolymer has a vinyl acetate content of at least 18% by weight. The concentrate is maintained in a moisture-free environment and is in solid form. The concentrates are used in the moisture cross-linking of alpha-olefin polymers and offer versatility in processes for such cross-linking.

Moisture cross-linking of polymers

A process for the dyeing of polymers of propylene, butene-1 and 4-methyl-pentent-1 is disclosed. The process involves contacting articles of the polymer with an aqueous dyebath containing a basic dye in a concentration of at least 0.4 g/l and at a pH of at least 5.0. The temperature of the aqueous dyebath is at least 90.degree. C. The article is maintained in contact with the dyebath for at least 10 minutes. The polymer of propylene is preferably a blend of 50-99 parts of a homopolymer of propylene or copolymer of propylene and ethylene with 1-50 parts of a zinc ionomer or graft copolymer of a hydrocarbon alpha-olefin with an alpha-olefin having carboxylic acid or carboxylic acid anhydride. Dyed polymers are obtained.

Process for the dyeing of polymers of propylene, butene-1 and

A continuous process for the dyeing of melt-extrudable polymers that are capable of being dyed, is disclosed. The process comprises extruding molten polymer through an orifice, contacting the extruded polymer while still in a molten state with an aqueous solution of a dye for said polymer, and withdrawing the resultant dyed polymer from the aqueous solution. The process may be used for the dyeing of e.g. modified polyolefins, polyamides, ionomers and the like. In preferred embodiments the process may be used in the extrusion coating of wire or other continuous filamentary material to provide color-coded products.

Continuous process for the dyeing of polymers

A polyolefin that has been modified with sulphur trioxide/trimethylamine complex is disclosed. The polyolefin may be homopolymer or copolymer of alpha-olefins selected from the group consisting of alpha-olefins having 2-10 carbons atoms, such alpha-olefins being hydrocarbon. Preferred polymers are homopolymers of ethylene or propylene, or copolymers of ethylene and at least one C.sub.3 -C.sub.10 alpha-olefin. The modified polyolefin is preferably formed by admixing molten polyolefin with 20-2000 ppm of the complex at a temperature of at least 210.degree. C. The modified polyolefin is dyeable.

Process for sulphonating molten polyolefins

A process for the dyeing of polymers of ethylene is disclosed. The process involves contacting articles of the polymer with an aqueous dyebath containing a basic dye in a concentration of at least 0.5 g/l and at a pH of at least 5.0. The temperature of the aqueous dyebath is at least 35.degree. C., especially at least 55.degree. C. The article is maintained in contact with the dyebath for at least 20 seconds. The polymer of ethylene is a blend of 65-99 parts of a homopolymer of ethylene or copolymer of ethylene and at least one C.sub.3 -C.sub.10 higher alpha-olefin with 1-35 parts of a direct or graft copolymer of an alpha-olefin having carboxylic acid, carboxylic acid anhydride, ionomeric or --OH groups. Dyed polymers of ethylene are obtained.

Process for dyeing of polymers of ethylene with basic dyes

A process for the recovery of a proteinaceous oat fraction from a dispersion thereof in an aliphatic hydrocarbon solvent is disclosed. The dispersion is admixed with at least 2.5%, by weight, of a solution of ethyl alcohol and water, whereby the dispersion agglomerates. The amount of water in the resultant admixture of agglomerate and solvent is then reduced to less than 0.3%, by weight. The proteinaceous oat fraction that is recovered has a low bulk density, e.g., less than 0.14 g/ml, is white, soft and fluffy. The fraction may be used in a variety of food products.

Recovery of a proteinaceous oat fraction from a dispersion thereof in

A process for the extraction of food values from oats is disclosed. Acid-soluble protein may be obtained by de-oiling comminuted groats, treating the de-oiled groats with an aqueous solution of pH 9.5-11.5, acidifying the alkaline solution after separation of insoluble material to a pH of 1.8-3.2, preferably 2.2-2.8, and separating acid-soluble protein from the acidified solution after separation of insoluble material. Each step in the process is controlled so as to minimize denaturing of acid-soluble protein. Techniques for separation of acid-soluble protein from the acidified solution are disclosed. The separation of other protein products, bran, flour and gum is also disclosed. The use of protein products as emulsifying agents is disclosed.

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Kingston, Canada

John R Boocock