Abstract: The present invention relates to fractional melt flow rate powders wherein the particles are substantially spherical in shape and range in size from about 10 up to about 200 microns. The invention also relates to a process whereby a dispersible olefin copolymer resin can be converted into a microfine powder with reduced melt index. The process entails dispersing a molten olefin copolymer resin containing silane functionality in a liquid medium in the presence of a nonionic surfactant and catalyst and, after the melt flow rate is reduced to the desired level, cooling the dispersion to below the melt point of the olefin polymer.

Abstract: The present invention relates to fractional melt flow rate powders wherein the particles are substantially spherical in shape and range in size from about 10 up to about 200 microns. The invention also relates to a process whereby a dispersible olefin copolymer resin can be converted into a microfine powder with reduced melt index. The process entails dispersing a molten olefin copolymer resin containing silane functionality in a liquid medium in the presence of a nonionic surfactant and catalyst and, after the melt flow rate is reduced to the desired level, cooling the dispersion to below the melt point of the olefin polymer.

Abstract: The present invention is directed to improved microfine propylene polymer powders having reduced fines which are comprised of spherical or substantially spherical particles and have a number average particle size from about 25 to about 60. A process for preparing the improved powders is also provided. The process involves dispersing a molten propylene homopolymer or copolymer which has been visbroken in a liquid medium in the presence of a nonionic surfactant, cooling the dispersion below the melt point of the propylene polymer and recovering the powder.

Abstract: The present invention relates to crosslinkable microfine ethylene copolymer powders which are substantially spherical in shape and range in size from about 10 up to about 500 microns and to the process of crosslinking the powders to reduce their melt flow rate. The powders are crosslinked by contacting with water in the presence of a silanol condensation catalyst at temperatures from ambient up to about 110.degree. C. The reduction in melt flow rate is accomplished without substantially changing the powder characteristics, i.e., particle size and particle size distribution.

Abstract: A process for preparing ionomers is disclosed. In this process a vinyl acetate polymer is contacted with a hydroxide of an alkali metal or an alkaline earth metal. The in situ formed acetate of an alkali metal or an alkaline earth metal of this reaction is in turn reacted with a polymer having carboxylic acid or diacid anhydride funtionality to produce the ionomer.

Abstract: An improved emulsion polymerization process for the preparation of high Mooney viscosity terpolymers of ethylene, vinyl acetate, and reactive halogen-containing monomers is provided. In the process, the reactive halogen-containing monomer is added during the polymerization. The ethylene pressure may also be increased during the polymerization.

Abstract: Interpolymers are provided which are based upon the interpolymerization of a vinyl ester of an alpha-unbranched saturated monocarboxylic acid, a monomer selected from the group consisting of an alkyl ester of an alpha, beta ethylenically unsaturated monocarboxylic acid and a vinyl ester of an alpha-branched saturated monocarboxylic acid and a vinylcyclopropanedicarboxylate polyester oligomer or mixture thereof. Optionally, an alpha, beta ethylenically unsaturated carboxylic acid may be added. The interpolymers are particularly useful for formulating surface coatings such as semi-gloss paints where they have been found to significantly improve the wet adhesion properties thereof.

Abstract: Interpolymers are provided which are based upon the interpolymerization of a vinyl ester, a lower alpha olefin, optionally an alpha, beta ethylenically unsaturated carboxylic acid and a vinylcyclopropanedicarboxylate polyester oligomer or mixtures thereof. The interpolymers are particularly useful for formulating latex adhesives where they have been found to significantly improve the creep resistance properties thereof.

Abstract: A process is disclosed for preparing copolymer latices possessing a solids content of at least about 60 weight percent and a viscosity not exceeding 15,000 cp. Brookfield Viscosity (RVF, Spindle No. 4) at 2 rpm from (a) vinyl acetate in an amount representing from about 10 weight percent to about 95 weight percent of total monomer charge, and (b) at least one monomer selected from the group consisting of acrylate ester, methacrylate ester and vinyl ester of an alpha-branched saturated monocarboxylic acid representing the balance of the total monomer charge.

Abstract: In a process for preparing an elastomeric vinyl acetate-ethylene copolymer having high Mooney viscosity and low gel content wherein vinyl acetate monomer is copolymerized with ethylene monomer in an aqueous emulsion reaction medium containing surface active agent, polymerization catalyst and protective colloid to provide a latex and vinyl acetate-ethylene elastomer is recovered from the latex, an improvement is disclosed which comprises:copolymerizing from about 40% to about 70% by weight of vinyl acetate monomer with from about 60% to about 30% by weight of ethylene monomer in an aqueous emulsion reaction medium to provide a latex, the reaction medium for vinyl acetate-ethylene elastomer containing:(i) at least one surface active agent having a hydrophilic lipophilic balance value of at least 22 in an amount above about 2.

Abstract: Vinyl acetate-ethylene copolymer latices having an inherent viscosity of not less than about 1.90 and demonstrating superior performance in the Time of Set Test and Vinyl Wetting Test are prepared by the process which comprises copolymerizing from about 60% to about 95% by weight of vinyl acetate monomer with from about 40% to about 5% by weight of ethylene monomer in an emulsified reaction medium containing:(a) at least one surface active agent in an amount of not less than about 1.0% by weight, and not more than about 2.0% by weight, of the total monomer,(b) a catalyst, and(c) a protective colloid,the total weight of the surface active agent and vinyl acetate monomer being introduced into the reaction medium in delayed increments prior to and after the commencement of copolymerization.