This invention provides a material having a low dissipation factor that is suitable for use as an insulating material for a printed wiring board and the like; a resin composition used for the production of the material; and an application using the material. The present invention relates to a resin composition comprising a mono(C.sub.6-C.sub.20 alkyl)diallyl isocyanurate and a polyphenylene ether resin; a cured product of the resin composition; and use of the cured product.

A method for preparing a poly(phenylene ether) includes feeding an oxygen-containing gas phase to a single continuous flow reactor containing a reaction mixture, and oxidatively polymerizing the reaction mixture to form a poly(phenylene ether) in the single reactor. The reaction mixture includes a phenol, a transition metal catalyst, and an organic solvent. A poly(phenylene ether) made by the method and articles including the poly(phenylene ether) are also disclosed. Methods for quantifying phenol concentration and poly(phenylene ether) molecular weight in the reaction mixture are also discussed.

A method for preparing a poly(phenylene ether) includes feeding an oxygen-containing gas phase to a single continuous flow reactor containing a reaction mixture, and oxidatively polymerizing the reaction mixture to form a poly(phenylene ether) in the single reactor. The reaction mixture includes a phenol, a transition metal catalyst, and an organic solvent. A poly(phenylene ether) made by the method and articles including the poly(phenylene ether) are also disclosed. Methods for quantifying phenol concentration and poly(phenylene ether) molecular weight in the reaction mixture are also discussed.

Disclosed is a method for synthesizing dihydroxyl-terminated polyphenylene oxide oligomer. The method for synthesizing dihydroxyl-terminated polyphenylene oxide oligomer, comprising oxidatively copolymerizing monohydric phenol and dihydric phenol in the presence of a metal-polyethyleneimine complex as a catalyst, to obtain the dihydroxyl-terminated polyphenylene oxide oligomer. The synthesizing method of the present disclosure uses a metal-polyethyleneimine complex as a catalyst, which has a milder catalytic activity, can effectively promote the reaction between the dihydric phenol and the monohydric phenol, increases the hydroxyl content of the product, meanwhile reduces the amount of the residual dihydric phenol monomer in the product, so that the quality of the product can be improved. The dihydroxyl-terminated polyphenylene oxide oligomer prepared can be used as additive and copolymerization block in other thermoplastic plastics, thermoplastic elastomers and thermosetting materials, thereby improving the performances of the material, such as thermal performance, adhesion, mechanical property, chemical resistance, and electrical property.

Disclosed is a method for synthesizing dihydroxyl-terminated polyphenylene oxide oligomer. The method for synthesizing dihydroxyl-terminated polyphenylene oxide oligomer, comprising oxidatively copolymerizing monohydric phenol and dihydric phenol in the presence of a metal-polyethyleneimine complex as a catalyst, to obtain the dihydroxyl-terminated polyphenylene oxide oligomer. The synthesizing method of the present disclosure uses a metal-polyethyleneimine complex as a catalyst, which has a milder catalytic activity, can effectively promote the reaction between the dihydric phenol and the monohydric phenol, increases the hydroxyl content of the product, meanwhile reduces the amount of the residual dihydric phenol monomer in the product, so that the quality of the product can be improved. The dihydroxyl-terminated polyphenylene oxide oligomer prepared can be used as additive and copolymerization block in other thermoplastic plastics, thermoplastic elastomers and thermosetting materials, thereby improving the performances of the material, such as thermal performance, adhesion, mechanical property, chemical resistance, and electrical property.

An oligomer (2,6-dimethylphenylene ether) is provided. Its structure is shown as follows:

##STR00001##

which comprises separately independent hydrogen; alkyl or phenyl; separately independent —NR—, —CO—, —SO—, —CS—, —SO.sub.2—, —CH.sub.2—, —O—, null, —C(CH.sub.3).sub.2—, or

##STR00002##

and a hydrogen,

##STR00003##

The features of the cured products include a high glass-transition temperature, a low dielectric feature, preferred thermal stability, and good flame retardancy. The present invention effectively controls the number-average molecular weight of the product to obtain excellent organic solubility.

An oligomer (2,6-dimethylphenylene ether) is provided. Its structure is shown as follows:

##STR00001##

which comprises separately independent hydrogen; alkyl or phenyl; separately independent —NR—, —CO—, —SO—, —CS—, —SO.sub.2—, —CH.sub.2—, —O—, null, —C(CH.sub.3).sub.2—, or

##STR00002##

and a hydrogen,

##STR00003##

The features of the cured products include a high glass-transition temperature, a low dielectric feature, preferred thermal stability, and good flame retardancy. The present invention effectively controls the number-average molecular weight of the product to obtain excellent organic solubility.

A resin comprises at least one compound selected from one of the following formulas ##STR00001##

A resin comprises at least one compound selected from one of the following formulas ##STR00001##

A method for producing polyphenylene ether amine includes following steps. In step (a), a hydrogenation reaction tank is provided; a guided gas stirrer is disposed in the hydrogenation reaction tank. In step (b), a reaction solution is placed in the hydrogenation reaction tank, and the reaction solution is nitro polyphenylene ether dissolved in a solvent. In step (c), a hydrogenation catalyst is added to the reaction solution. In step (d), a hydrogen gas is introduced into the hydrogenation reaction tank. In step (e), the guided gas stirrer is activated. In step (f), a hydrogenation reaction is carried out on the conditions that a reaction temperature is 50-200° C. and a reaction time is 1-20 hours, so as to hydrogenate the nitro polyphenylene ether in the reaction solution to polyphenylene ether amine. In step (g), the reaction solution is cooled down to a room temperature; the hydrogenation catalyst is removed.