C08G75/0231

POLYARYLENE SULFIDE RESIN, METHOD FOR PRODUCING SAME, POLY(ARYLENE SULFONIUM SALT), AND METHOD FOR PRODUCING POLY(ARYLENE SULFONIUM SALT)

Disclosed is a production method comprising a step of obtaining a poly(arylene sulfonium salt) comprising a terminal group including at least one functional group selected from the group consisting of a carboxy group, a hydroxy group and an amino group, and a step of dealkylating or dearylating the poly(arylene sulfonium salt) to obtain a polyarylene sulfide resin, and a polyarylene sulfide resin comprising a terminal group including a functional group obtainable by the production method.

POLYARYLENE SULFIDE RESIN, METHOD FOR PRODUCING SAME, POLY(ARYLENE SULFONIUM SALT), AND METHOD FOR PRODUCING POLY(ARYLENE SULFONIUM SALT)

Disclosed is a production method comprising a step of obtaining a poly(arylene sulfonium salt) comprising a terminal group including at least one functional group selected from the group consisting of a carboxy group, a hydroxy group and an amino group, and a step of dealkylating or dearylating the poly(arylene sulfonium salt) to obtain a polyarylene sulfide resin, and a polyarylene sulfide resin comprising a terminal group including a functional group obtainable by the production method.

BRANCHED POLYARYLENE SULFIDE RESIN, METHOD FOR MANUFACTURING SAME AND USE AS POLYMER MODIFIER
20180044477 · 2018-02-15 · ·

A branched polyarylene sulfide resin includes an S substituent group with a cleaved disulfide compound, which has a halogen content of 4,000 ppm or less, a melt viscosity as measured at a temperature of 330 C. and a shear rate of 2 sec.sup.1 of 1.010.sup.4 to 50.0 x 10.sup.4 Pa.Math.s, and a melt viscoelasticity tan as measured at a temperature of 310 C. and an angular velocity of 1 rad/sec of 0.1 to 0.6.

BRANCHED POLYARYLENE SULFIDE RESIN, METHOD FOR MANUFACTURING SAME AND USE AS POLYMER MODIFIER
20180044477 · 2018-02-15 · ·

A branched polyarylene sulfide resin includes an S substituent group with a cleaved disulfide compound, which has a halogen content of 4,000 ppm or less, a melt viscosity as measured at a temperature of 330 C. and a shear rate of 2 sec.sup.1 of 1.010.sup.4 to 50.0 x 10.sup.4 Pa.Math.s, and a melt viscoelasticity tan as measured at a temperature of 310 C. and an angular velocity of 1 rad/sec of 0.1 to 0.6.

Dual cure sealants

Compositions that are curable by free radical redox reactions are disclosed. Free radical curing reactions between polythiols and polyalkyenyls are initiated by the reaction of metal complexes and organic peroxides. The compositions are useful as sealants.

Dual cure sealants

Compositions that are curable by free radical redox reactions are disclosed. Free radical curing reactions between polythiols and polyalkyenyls are initiated by the reaction of metal complexes and organic peroxides. The compositions are useful as sealants.

Polyarylene sulfide production method

A method for producing polyarylene sulfide that can have a high melt viscosity while suppressing ultra-fine powder generation. The method for producing polyarylene sulfide includes: (1) preparing a prepared mixture containing an organic polar solvent, a sulfur source, and a dihalo aromatic compound; (2) initiating a polymerization reaction by heating the prepared mixture to produce a prepolymer; (3) adding water as a phase separation agent to a reaction mixture in a reaction system to form a phase-separated state; and (4) continuing the polymerization reaction after phase separation. In the method, when a dihalo aromatic compound conversion ratio is 80 mass % or greater and 93 mass % or less and after the prepolymer reaches a weight average molecular weight of 10000 or greater in the first-stage polymerization step, an aromatic compound having 3 or more halogen atoms bonded to an aromatic ring is added to the reaction mixture.

Polyarylene sulfide production method

A method for producing polyarylene sulfide that can have a high melt viscosity while suppressing ultra-fine powder generation. The method for producing polyarylene sulfide includes: (1) preparing a prepared mixture containing an organic polar solvent, a sulfur source, and a dihalo aromatic compound; (2) initiating a polymerization reaction by heating the prepared mixture to produce a prepolymer; (3) adding water as a phase separation agent to a reaction mixture in a reaction system to form a phase-separated state; and (4) continuing the polymerization reaction after phase separation. In the method, when a dihalo aromatic compound conversion ratio is 80 mass % or greater and 93 mass % or less and after the prepolymer reaches a weight average molecular weight of 10000 or greater in the first-stage polymerization step, an aromatic compound having 3 or more halogen atoms bonded to an aromatic ring is added to the reaction mixture.