Abstract:
An improved polymer devolatilization apparatus comprising a flat plate heater (22) comprising a polymer solution supply means (20), and a liquid/vapor collection and separation means, said flat plate heater further comprising a multiplicity of flat plates defining a plurality of channels (10), each channel having a substantially uniform height, but varying width over the total channel length, each channel comprising three zones: a first zone (12), having a beginning (18) and a terminus, said beginning in operative communication with the polymer solution supply means, characterized by decreasing width as a function of distance from its beginning, a second zone (14) having a beginning at the terminus of the first zone and a terminus, characterized by at least one occurrence of a restrictive cross-sectional area, and a third zone (16) having a beginning at the terminus of the second zone and terminating at a liquid/vapor collection and separation region operating at reduced pressure, said third zone characterized by increasing width as a function of distance from its beginning, and provided further that the ratio of maximum width of the third zone to the maximum width of the second zone is from 2:1 to 20:1.
Abstract:
A process for preparing glutarimide resins by the amidization and cycloimidization of methacrylate resins in the presence of a solvent characterized in that the solvent consists essentially of cyclohexanol.
Abstract:
A process for preparing halogenated polycarbonate wherein the total amount of base, the end pH of the aqueous phase, and the amount of coupling catalyst employed in the reaction are controlled to selected levels. In one embodiment, carbonate oligomers are condensed to form polycarbonate by contacting said oligomers in a tank reactor with an (i) organic solvent; (ii) 50 weight parts per million or less of coupling catalyst, based on the weight of all organic solvent employed in the oligomer formation and condensation steps, including any in which the coupling catalyst may be dissolved; and (iii) an amount of base which, together with the amount of base employed in the oligomer formation step, brings the total moles of base employed in the oligomer formation and condensation steps per mole of dihydroxy compound to the number given by 2 + 4(Y-1) + Q, where Y is the number of moles of carbonate precursor per mole of dihydroxy compound, and Q is about 0.001 to about 0.2. In another embodiment, carbonate oligomers are condensed to form polycarbonate by contacting said oligomers in a tubular reactor with an (i) organic solvent; (ii) 150 weight parts per million or less of coupling catalyst, based on the weight of all organic solvent employed in the oligomer formation and condensation steps, including any in which the coupling catalyst may be dissolved; and (iii) an amount of base which, together with the amount of base employed in the oligomer formation step, brings the total moles of base employed in the oligomer formation and condensation steps per mole of dihydroxy compound to the number given by 2 + 4(Y-1) + Q, where Y is the number of moles of carbonate precursor per mole of dihydroxy compound, and Q is about 0.001 to about 0.5. The process yields a halogenated polycarbonate of desirably high weight molecular weight, for example in excess of 80,000.
Abstract:
A process for producing a monovinylidene aromatic polymer having molecular weight (Mw) greater than 275,000 which comprises polymerizing a monomer mixture comprising a monovinylidene aromatic monomer in the presence of: A) from 10 to 2000 ppm by weight of at least one free radical generating, branching polymerization initiator; and B) from 10 to 2000 ppm of one or more organic gel reduction agent selected from the group consisting of: 1) mercaptans, terpenes, halocarbons and halohydrocarbons, such agent having up to 20 carbons; 2) distillate recovered from the reaction devolatilization process (recycle); and 3) mixtures of 1) and 2).