Patent classifications
C08F2/24
LATEXES WITH PH RESPONSIVE RESIN PARTICLES
Latexes are provided which may comprise water and resin particles comprising a polymerization product of reactants comprising a dioxane/dioxolane monomer and an additional monomer, wherein the dioxane/dioxolane monomer is an ester of (meth)acrylic acid with an alcohol comprising a dioxane moiety, an ester of (meth)acrylic acid with an alcohol comprising a dioxolane moiety, or both.
LATEXES WITH PH RESPONSIVE RESIN PARTICLES
Latexes are provided which may comprise water and resin particles comprising a polymerization product of reactants comprising a dioxane/dioxolane monomer and an additional monomer, wherein the dioxane/dioxolane monomer is an ester of (meth)acrylic acid with an alcohol comprising a dioxane moiety, an ester of (meth)acrylic acid with an alcohol comprising a dioxolane moiety, or both.
Surfactant composition
The polymerization stability and the chemical stability and the water resistance of resin films are improved. A surfactant composition according to an embodiment contains a surfactant (A) represented by general formula (1) and an anionic surfactant (B) having a hydrophobic group different from that of the surfactant (A). In the formula, R.sup.1 represents one or two groups selected from groups below, D.sup.1 represents a polymerizable unsaturated group represented by chemical formula D.sup.1-1 or D.sup.1-2 below, R.sup.2 represents a hydrogen atom or a methyl group, m1 and m2 represent 1 to 2, A.sup.1 represents an alkylene group with 2 to 4 carbon atoms, and m3 represents 1 to 100. ##STR00001##
METHOD FOR POLYMERISING ETHYLENICALLY UNSATURATED MONOMERS
The invention relates to a method for polymerising ethylenically unsaturated monomers by free-radical initiated emulsion polymerisation in an aqueous medium in a polymerisation reactor, wherein the inside walls and optionally also the fittings in the reactor are coated by applying a deposit-inhibiting product before the reactor is filled, characterised in that the surfaces that are to be coated with deposit-inhibiting product are treated with an acid solution.
VINYL CHLORIDE-VINYL ACETATE COPOLYMER AND METHOD OF PREPARING THE SAME
The present invention relates to a vinyl chloride-vinyl acetate copolymer, which may exhibit excellent tensile strength even during low-temperature processing, and a method of preparing the same. The copolymer according to the present invention may exhibit excellent tensile strength even during low-temperature processing by including a vinyl acetate-derived unit in a specific ratio and having a specific range of polydispersity index, for example, a polydispersity index of 2.1 to 2.4, at a degree of polymerization of 1,200 to 1,300. Thus, the vinyl chloride-vinyl acetate copolymer according to the present invention and the method of preparing the same may be easily applied to industries that need them, particularly, automotive industry or polyvinyl chloride resin industry.
POLYVINYL BUTYRAL DISPERSIONS
A stable aqueous film forming dispersion comprising:
a polymer selected from the group consisting of: polyvinyl butyral, polyvinyl acetyl, ethylene vinyl acetate, vinyl acetate and mixtures thereof:
a plasticiser;
an emulsifier; and
a water soluble organometallic crosslinking agent.
POLYVINYL BUTYRAL DISPERSIONS
A stable aqueous film forming dispersion comprising:
a polymer selected from the group consisting of: polyvinyl butyral, polyvinyl acetyl, ethylene vinyl acetate, vinyl acetate and mixtures thereof:
a plasticiser;
an emulsifier; and
a water soluble organometallic crosslinking agent.
Continuous inverse emulsion polymerization process for uniform polymer size distribution
A continuous inverse emulsion polymerization process may involve combining an aqueous monomer composition with an oil composition in a premix vessel and allowing the aqueous monomer composition to interact with the oil composition in the premix vessel for a period of time effective to form a stable pre-emulsion. The stable pre-emulsion may then be homogenized to form a homogenized emulsion that is then polymerized to form a water-in-oil inverse emulsion polymer. By forming a stable pre-emulsion that is then homogenized, the resulting water-in-oil inverse emulsion polymer may have uniform and consistent polymer size distribution.
Continuous inverse emulsion polymerization process for uniform polymer size distribution
A continuous inverse emulsion polymerization process may involve combining an aqueous monomer composition with an oil composition in a premix vessel and allowing the aqueous monomer composition to interact with the oil composition in the premix vessel for a period of time effective to form a stable pre-emulsion. The stable pre-emulsion may then be homogenized to form a homogenized emulsion that is then polymerized to form a water-in-oil inverse emulsion polymer. By forming a stable pre-emulsion that is then homogenized, the resulting water-in-oil inverse emulsion polymer may have uniform and consistent polymer size distribution.
AQUEOUS LATEX OF VINYLIDENE CHLORIDE COPOLYMER
Aqueous latex of vinylidene chloride copolymer An aqueous latex [latex (L)] of a vinylidene chloride copolymer [copolymer (A)], wherein the copolymer (A) consists essentially of recurring units derived from vinylidene chloride (VDC) in an amount comprised between 89.0 and 91.0 wt % of the copolymer, recurring units derived from methacrylonitrile (MAN) in an amount comprised between 2.00 and 5.50 wt % of the copolymer, recurring units derived from at least one ionic comonomer (ICO) in an amount comprised between 0.5 and 1.4 wt % of the copolymer (A), and recurring units derived from methylmethacrylate (MMA) in an amount such that the total of recurring units of VDC, MAN, ICO and MMA is 100 wt %, and wherein the latex (L) comprises at least one surfactant [surfactant (S)] in an amount comprised between 0.09 and 1.50 wt % of the copolymer (A).
Process for the manufacture of the aqueous latex (L), film made therefrom and retort pouch prepared with such film.