Abstract: The invention concerns processes for the production of multiarmed star copolymers comprising polymerizing vinyl chloride with a multifunctional initiator in the presence of Na2S2O4 and water. The invention also concerns polymers made from the processes and articles made from the polymers.

Abstract: Polyvinyl chloride reactor wall scale is reduced by conducting the polymerization in the presence of a phenothiazine dimer or higher oligomer made by reacting an aldehyde such as acetaldehyde or benzaldehyde with phenothiazine, or by reacting 2-acetylphenothiazine with formaldehyde.

Abstract: A microsuspension polymerization process for polymerizing vinyl chloride and optional comonomers to polyvinyl chloride and optional copolymers is disclosed which comprises conducting the polymerization in a tubular reaction zone without agitation in the presence of a compound having the formula ##STR1##

Abstract: A composition having the formula ##STR1## wherein n has an average value of one to about five, is disclosed for use in reducing or eliminating the formation of reactor scale during the polymerization of vinyl chloride and comonomers. The composition is prepared by reacting phenothiazine with formaldehyde in the presence of a liquid diluent that is a solvent for the phenothiazine, but a non-solvent for the dimer of phenothiazine and formaldehyde. The process of the invention is preferably conducted in the presence of a strong acid catalyst. The formaldehyde is preferably added slowly to the reaction mixture over the course of the reaction. The product can be filtered and dried.

Abstract: A composition having the formula ##STR1## wherein n has an average value of one to about five, is disclosed for use in reducing or eliminating the formation of reactor scale during the polymerization of vinyl chloride and comonomers. The composition is prepared by reacting phenothiazine with formaldehyde in the presence of a liquid diluent that is a solvent for the phenothiazine, but a non-solvent for the dimer of phenothiazine and formaldehyde. The process of the invention is preferably conducted in the presence of a strong acid catalyst. The formaldehyde is preferably added slowly to the reaction mixture over the course of the reaction. The product can be filtered and dried.

Abstract: A composition having the formula ##STR1## wherein n has an average value of one to about five, is disclosed for use in reducing or eliminating the formation of reactor scale during the polymerization of vinyl chloride and comonomers. The composition is prepared by reacting phenothiazine with formaldehyde in the presence of a liquid diluent that is a solvent for the phenothiazine, but a non-solvent for the dimer of phenothiazine and formaldehyde. The process of the invention is preferably conducted in the presence of a strong acid catalyst. The formaldehyde is preferably added slowly to the reaction mixture over the course of the reaction. The product can be filtered and dried.

Abstract: Spherical particles of vinyl resins having high bulk density can be prepared by the suspension polymerization process by using as a dispersant an alkyl hydroxy cellulose having a viscosity of from about 1000 to about 100,000 cps. A suitable dispersant is a hydroxypropyl methyl cellulose polymer having the formula: ##STR1## where n is from about 300 to about 1500.

Abstract: Spherical particles of vinyl resins having high bulk density can be prepared by the suspension polymerization process by using as a dispersant an alkyl hydroxy cellulose having a viscosity of from about 1000 to about 100,000 cps. A suitable dispersant is a hydroxypropyl methyl cellulose polymer having the formula: ##STR1## where n is from about 300 to about 1500.

Abstract: This invention relates to a process of producing vinyl polymers by an inversion polymerization technique in the presence of a coating on the internal surfaces of the polymerization reactor. The coating on said surfaces may be a singular layer or a dual layer coating. By inversion polymerization is meant conducting the initial stage of the polymerization reaction in a medium wherein the monomer or monomers being polymerized constitute the continuous phase and in the second or later stage of polymerization, water constitutes the continuous phase. The principal coating, or undercoating when a dual layer coating is employed, comprises a protein, such as egg albumen, and when a top coating is used it comprises a water-soluble suspending agent, such as an alkyl or alkyl hydroxyalkyl cellulose ether. When polymerizing olefinic monomers, such as vinyl halides, vinylidene halides, and vinylidene monomers having at least one terminal CH.sub.2 .dbd.

Abstract: This invention relates to a process of producing vinyl polymers or resins by an inversion polymerization technique in the presence of a dual layer coating on the internal surfaces of the polymerization reactor. By inversion polymerization is meant conducting the polymerization reaction in two stages, in the first or initial stage of which the monomer or monomers being polymerized constitute the continuous phase, and in the second or latter stage of polymerization, water constitutes the continuous phase due to the addition of sufficient water to the reactor to form said phase. The dual layer coating comprises an undercoating or primary coating of a tannin or tannate such as tannic acid or ammonium tannate, said coating being applied from an aqueous solution thereof, and a top coating comprised of a water-soluble suspending agent, such as an alkyl or an alkyl hydroxyalkyl cellulose ether, said top coating being applied from an aqueous solution thereof.

Abstract: This invention relates to a process of producing vinyl polymers or resins by an inversion polymerization technique in the presence of a dual layer coating on the internal surfaces of the polymerization reactor. By inversion polymerization is meant conducting the polymerization reaction in two stages, in the first or initial stage of which the monomer or monomers being polymerized constitute the continuous phase, and in the second or latter stage of polymerization, water constitutes the continuous phase due to the addition of sufficient water to the reactor to form said phase.