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36results about How to "Extend polymerization time" patented technology

Furan dicarboxylic acid copolyester and preparation method thereof

The invention relates to furan dicarboxylic acid copolyester and a preparation method thereof. The preparation method comprises the following steps: mixing a first component, a second component and athird component with the mole ratio of 1 to (1.1 to 2.0) to (0.0001 to 0.02) with an esterification catalyst to obtain a first intermediate product, wherein the first component comprises at least oneof furan dicarboxylic acid and a furan dicarboxylic acid ester compound, the second component comprises at least one of aromatic diol and aliphatic diol, and the third component comprises polyhydric alcohol with hydroxyl number being greater than or equal to 3; performing prepolymerization reaction and polycondensation on the first intermediate product to obtain the furan dicarboxylic acid copolyester. In the preparation method, the polyhydric alcohol with hydroxyl number being greater than or equal to 3 serves as a connection point of chain segments, so that the chain segment structure of thefuran dicarboxylic acid copolyester is expanded to a network structure, thereby obtaining the colorless or lightcolor furan dicarboxylic acid copolyester with excellent mechanical property and air barrier property and high molecular weight.
Owner:NINGBO INST OF MATERIALS TECH & ENG CHINESE ACADEMY OF SCI

Laminated polyester film for protective material for protecting back surface of photovoltaic cells

The present invention provides a polyester film for a protective material for protecting a back surface of photovoltaic cell which exhibits a good hydrolysis resistance and an excellent adhesion property to a sealing resin for photovoltaic cells. The present invention relates to a polyester film for a protective material for protecting a back surface of photovoltaic cells which is in the form of a laminated polyester film comprising the below-mentioned polyester (A) layer as at least one of outermost layers of the film and at least one below-mentioned polyester (B) layer, the laminated polyester film having a terminal carboxyl group content of not more than 26 equivalents/t, and the polyester (A) layer being provided on at least one surface thereof with a coating layer formed of a polyurethane having at least one of a polycarbonate skeleton and a polyether skeleton, and a crosslinking agent:
    • Polyester (A) layer: Layer formed of a polyester comprising an aromatic polyester as a main constitutional component and having a white pigment content of less than 8% by weight; and
    • Polyester (B) layer: Layer formed of a polyester comprising an aromatic polyester as a main constitutional component and having a white pigment content of not less than 8% by weight.
Owner:MITSUBISHI PLASTICS INC

Furyl copolyester and preparation method thereof

The invention relates to furyl copolyester and a preparation method thereof. The preparation method comprises the following steps: mixing a first component, a second component and a third component with the mole ratio of 1 to (1.1 to 2.0) to (0.0001 to 0.02) with an esterification catalyst to obtain a first intermediate product, wherein the first component comprises at least one of furan dicarboxylic acid and a furan dicarboxylic acid ester compound, the second component comprises at least one of aromatic diol and aliphatic diol, and the third component comprises acid anhydride with carbonyl number being greater than or equal to 3; performing prepolymerization reaction and polycondensation on the first intermediate product to obtain furyl copolyester. In the preparation method, the acid anhydride with carbonyl number being greater than or equal to 3 serves as a connection point of chain segments, so that the chain segment structure of the furyl copolyester is expanded to a network structure, thereby obtaining the colorless or lightcolor furyl copolyester with excellent mechanical property and air barrier property and high molecular weight, and further meeting the application requirement of furyl copolyester in the fields of packing materials, thin films, fibers, engineering plastics and the like.
Owner:NINGBO INST OF MATERIALS TECH & ENG CHINESE ACADEMY OF SCI

Delay type high-centipoise molecule dynamic synthesis device

The invention relates to a delay type high-centipoise molecule dynamic synthesis device which is suitable for the field of macromolecule polymerization, and especially suitable for high-centipoise macromolecule synthesis. The delay type high-centipoise molecule dynamic synthesis device has the main structure as follows: firstly, a mixer is arranged in a dynamic synthesis device body, an upper-guiding blade is arranged at the upper end of a mixing shaft of the mixer, a dispersing blade is arranged at the lower end of the mixing shaft of the mixer; secondly, a monomer unit, a catalytic medium inlet, a heating medium inlet and a solvent inlet are formed in the bottom end of the dynamic synthesis device body, and are hollow pipelines; the tail ends of the pipelines all point to the position of a center shaft of the mixer, and also point to the edge of the dispersing blade at the lower end of the mixer. When the delay type high-centipoise molecule dynamic synthesis device works, each monomer, medium, solvent and catalyst are injected from respective inlets, and collected to the center shaft of the mixer or the edge of the dispersing blade, fully mixed and dispersed by the dispersing blade and polymerized, and guided to the upper end of a reaction kettle by the upper-guiding blade after the polymerization is completed within a short time, and output through a discharging hole.
Owner:王仲明

Method for controlling the temperature of butyl rubber reactor

ActiveCN105566544BGuaranteed gasificationUniform gasificationTemperature controlInstability
The invention provides a method for controlling temperature of a butyl rubber reactor. The method includes the steps that signals of a pressure transmitter of an ethylene tank are fed back to adjust a pressure regulating valve of the ethylene tank, the pressure of the ethylene tank is controlled below first pressure, the liquid column pressure difference value between normal ethylene liquid level elevation and heat exchange tube bundle top elevation of the reactor is subtracted from ethylene vapourizing pressure below minus 100 DEG C, and the obtained difference value and an adjusting margin value between the pipeline resistance drop from an outlet of the ethylene tank to an inlet of a heat exchange tube bundle of the reactor and a 10KPa adjustable decompression element are added to obtain the first pressure value; pressure drop of the adjustable decompression element is adjusted, so that the pressure of ethylene entering the heat exchange tube bundle of the reactor is equal to the ethylene vaporizing pressure below minus 100 DEG C. The method ensures that reactions are conducted stably below minus 100 DEG C, prolongs polymerization time, reduces the probability of reaction unexpected interrupt, improves productivity and production efficiency and reduces instability of the polymerization process. The method is simple in technological flow path and easy to operate, high in control accuracy, low in operation cost and safe and reliable in production, installation is convenient, and energy does not need to be consumed in the process.
Owner:中石油吉林化工工程有限公司
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