Abstract: In a continuous process for producing olefin polymers by contacting olefin monomers with an initiator or catalyst in a polymerization zone, the improvement comprising contacting fast poisons in the feed with a scavenging agent in a scavenging zone under conditions such that no significant amount of polymerization occurs until said feed is contacted with the initiator or catalyst in a polymerization zone.

Abstract: In the oxidation-polycondensation of a monohydric phenol in a reaction vessel equipped with a reflux condenser, in the presence of a complex catalyst comprising a copper compound and an amine, while passing an oxygen-containing gas thereinto, an improvement is provided wherein the temperature of the oxygen-containing gas to be discharged through the reflux condenser is adjusted to a range of 10.degree.-25.degree. C. to adequately maintain the balance of an amine and water during the course of the reaction. According to this improvement, the reaction advances well although a small amount of the amine escapes outside the reaction system along with a part of water resulting from the reaction. Further, the polymerization reaction can be repeated in a very stabilized state without any fluctuation of reaction time unlike the conventional method wherein the discharged gas through the reflux condenser is deeply cooled down to a temperature lower than 0.degree.C.

Abstract: A system for controlling the percent of polymer in a reactor in a process in which the reactor effluent, comprising a mixture of polymer, unreacted materials and, possibly, by-products, goes through a separator to remove from such effluent unreacted materials and by-products. The system is especially useful with variable fillage, horizontal continuous stirred tank reactors.

Abstract: A composition is described, useful as a thermoformable polymer, for producing shaped articles having high yield and impact strengths, good heat resistance, and good solvent resistance. The composition, which is cured, contains a crosslinked polycyanurate network polymer in which a high molecular weight thermoplastic polymer, such as a polyestercarbonate, is finely dispersed. The composition possesses a Vicat softening temperature (ASTM 1525) of at least about 10.degree. C. above that of said thermoplastic polymer alone, and an elongation-at-break value (ASTM D-638, at room temperature) at least twice that of said crosslinked polymer alone. Due to the high yield strength, lighter structural articles and components can be fabricated from the composition possessing high structural strength.

Abstract: Copolymers consisting of bisphenol-A ("BPA"), terephthalate ("TP"), and carbonate moieties in mol ratio from 2:0.8:1.2 to 2:1.3:0.7, which are melt processable in the sense of (a) showing no more than 10% change in viscosity number upon compression molding for 10 minutes at 320.degree. C. to form a plaque, (b) developing, in 2% (gm./ml.) DCM solution, a "yellowness index" of no more than 10 as observed by ASTM Test No. D-1925, using a 2 cm. path length; which copolymers approximate in properties the alternating copolymer consisting of the above moieties, as indicated by their having viscosity numbers ("I.V.") in the range between 0.6 and 1.5 dl./gm. and T.sub.G of 170.degree. to 194.degree. C., with T.sub.G vs. I.V. relationship conforming to the formula, T.sub.G =192-(11.5/I.V.)+9 and with difference of (T.sub.G -HDT) of not over 15.degree. C.; having Izod impact resistance (ft.-lb. per inch of notch) at 25.degree. C. of at least 5; and being essentially free of pyridine and of anhydride linkages.

Abstract: A process for producing a cyclopentadiene resin by heat copolymerizing a cyclopentadiene monomer and a comonomer copolymerizable therewith, which comprises(a) using a vinyl monomer containing an ester linkage or a hydroxyl group as the comonomer, and(2) feeding the polymerizable ingredients and optionally an inert solvent from a material-preparing zone to a polymerization zone to polymerize the polymerizable ingredients, feeding the polymer solution formed in the polymerization zone into a separating zone to separate a low-boiling mixture consisting of the unreacted monomers, a by-product oil and optionally the inert solvent from the resulting cyclopentadiene resin, and recycling at least a part of the separated low-boiling mixture to the material-preparing zone for use as a polymerizable ingredient.

Abstract: A process for preparing certain halogenated aromatic polyesters having a predetermined molecular weight is provided. Such polyesters are prepared by solution polymerization of an appropriate bisphenol and diacid halide wherein the diacid halide is added to a solution containing the bisphenol until the viscosity of the resulting polymer containing solution reaches a predetermined solution viscosity limit at which time the further addition of diacid halide is terminated. The solution viscosity limit is indicative of the attainment of said predetermined molecular weight. The identification of said solution viscosity limit is achieved by a feedback mechanism wherein the viscosity of the polymer containing solution is monitored or sensed during or after the addition of the diacid halide to the bisphenol containing solution.

Abstract: A method for detecting impending failure of suspension during an aqueous suspension polymerization has been developed by continuous monitoring of the electrical conductivity of the suspension system. A sudden drop in conductance warns of failure of suspension in time to save the suspension by the addition of suspension stabilizers. A special conductivity cell has been developed to allow measurement of conductance during the course of the polymerization reaction.

Abstract: Homopolymers and copolymers of vinyl chloride are produced in the form of a powder by a bulk polymerization process which involves a dual temperature operation. Vinyl chloride (either alone or admixed with other copolymerizable monomers) is contacted with conventional polymerization initiators in the absence of solvents or diluents at a first temperature of from about 68.degree. to about 110.degree. F until the polymerization has proceeded to 0.1 to 10% of completion and thereafter the temperature is raised to 120.degree. to 150.degree. F until the polymerization has reached the desired conversion.

Abstract: A method of measuring the extent of an exothermic chemical reaction while the reaction is proceeding which comprises measuring the difference between the ingoing and outgoing temperatures of a coolant passing through the reaction vessel and computing therefrom the heat produced by the reaction, and in which the numerical value of the temperature of the ingoing coolant is retained in a memory device before being compared with that of the outgoing coolant, the period of retention being equal to the time taken for coolant to pass from the point of measurement of the ingoing temperature to the point of measurement of the outgoing temperature. This corrects errors due to variations with time of the temperature of the ingoing coolant.

Abstract: A process for the preparation of a graft copolymer which comprises reacting (I) a hydrocarbon resin based on cyclopentadiene or methylcyclopentadiene or both at an elevated temperature with (II) an olefinically unsaturated polycarboxylic acid compound and (III) a copolyerisable unsaturated monomer in a manner such that for at least a part of the reaction the unsaturated monomer (III) and the polycarboxylic acid compound (II) are simultaneously present, a graft-polymer based on I. a hydrocarbon resin based on cyclopentadiene or methylcyclopentadiene or on both as essential monomers, II. olefinically unsaturated polycarboxylic acid compounds and III. copolymerisable unsaturated monomers and a printing ink which comprises, as at least part of the binder component, said polymer, a pigment and a solvent.