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133results about How to "Low gel content" patented technology

High-molecular weight long-chain branched crystalline polylactic acid material and preparation method thereof

The invention discloses a high-molecular weight long-chain branched crystalline polylactic acid material and a preparation method thereof. The preparation method comprises the following steps of: 1) adding 0.1 to 1 percent of protonic acid catalyst into aqueous solution of lactic acid or mixed solution of the aqueous solution of the lactic acid and silicon dioxide nano particle silica sol containing 0.1 to 10 weight percent of lactic acid, and dehydrating to obtain a product I; 2) adding 0.4 to 2 molar percent of dibasic acid or anhydride into the product I, and reacting to obtain a product II; 3) adding 0.1 to 1 weight percent of lewis acid catalyst into the product II, performing melt polycondensation, and adding 0.1 to 5 weight percent of crystallization accelerator to obtain terminal carboxyl group crystalline polylactic acid prepolymers; and 4) reacting diglycidyl ester and the terminal carboxyl group crystalline polylactic acid prepolymers in a molar ratio of 0.8:1-1.2:1 to obtain the high-molecular weight long-chain branched crystalline polylactic acid material. The preparation method has the advantages of simplicity, short reaction time, high efficiency, low cost and environmental friendliness and capability of contributing to realizing commercialization.
Owner:ZHEJIANG UNIV

Polypropylene for foam and polypropylene foam

The present invention is concerned with a polypropylene composition comprising a polypropylene base resin, the polypropylene composition having—a XHU content of less than 1.25 wt. %;—a F30 melt strength of at least 30 cN, determined in the Rheotens test at 200° C.; and—a melt extensibility v30 of at least 200 m / s, determined in the Rheotens test at 200° C. In another aspect the present invention is concerned with a polypropylene composition having an MFR (2.16 kg, 230° C., ISO 1133) of 1.0 to 5.0 g / 10 min comprising a polypropylene base resin, the polypropylene base resin being obtainable by producing an intermediate polypropylene having an MFR (2.16 kg, 230° C., ISO 1133) of 0.5 to 2.5 g / 10 min in the presence of an asymmetric catalyst; mixing the intermediate polypropylene with peroxide and at least one diene at a temperature of 20 to 90° C. for at least 2 minutes to form a pre-mixed material; melt mixing the pre-mixed material in a melt mixing device at a barrel temperature in the range of 180 to 300° C., whereby the melt mixing device is a melt mixing device includes a feed zone, a kneading zone and a die zone, whereby an initial barrel temperature T1 is maintained in the feed zone, a barrel temperature T2 is maintained in the kneading zone and a die barrel temperature T3 is maintained in the die zone, whereby the barrel temperatures T1, T2, and T3 satisfy the following relation: T1<T3<T2. In yet another aspect the present invention is concerned with a process for the production of a polypropylene composition having—a XHU content of less than 1.25 wt. %;—a F30 melt strength of at least 30 cN, determined in the Rheotens test at 200° C.; and—a melt extensibility v30 of at least 200 m / s, determined in the Rheotens test at 200° C. whereby an asymmetric catalyst derived intermediate polypropylene having an MFR (2.16 kg, 230° C., ISO 1133) of 0.5 to 2.5 g / 10 min is mixed with peroxide and at least one diene at a temperature of 20 to 90° C. for at least 2 minutes to form a pre-mixed material; and the pre-mixed material is melt mixed in a melt mixing device at a barrel temperature in the range of 180 to 300° C. In yet another aspect the present invention is concerned with foam comprising the polypropylene composition according to the present invention. The present invention is further concerned with the use of the polypropylene composition for producing foamed articles.
Owner:BOREALIS AG

Preparation method of polyether ketone/sulfone high-temperature resistant material

The invention discloses a preparation method of a polyether ketone / sulfone high-temperature resistant material, which comprises the following steps that: firstly, a reactive monomer, a solvent and an inorganic alkali are put into a first reactor, are mixed at a temperature of 40 to 90 DEG C by stirring, and are dissolved; secondly, the mixture is transferred to a second reactor, is added with a water-carrying agent, and is stirred at a temperature of 150 to 280 DEG C to be subjected to salt formation dehydration; and a material after being subjected to salt formation dehydration is introducedinto a third reactor, and is stirred at a temperature of 230 to 330 DEG C to be subjected to polymerization to obtain a product. The synthesis process of the polyether ketone / sulfone material is reacted in three reactors with different temperatures, so that an intermediate product prepared in each step is more sufficient and uniform, the obtained product has a gel content reduced to less than 3% and molecular weight distribution which is more reasonable and reaches the range of 2.42 to 2.45 without changing the comprehensive performance of the product, and thereby the quality of the resin product is improved; and the preparation method is suitable for continuous production, and production cost reduction, energy consumption reduction in a production process and stable quality of the obtained product are achieved.
Owner:KINGFA SCI & TECH CO LTD +2

High-nitrile SAN resin and production method thereof

The invention relates to a production method of high-nitrile SAN resin. The method comprises the specific steps of (a) mixing acrylonitrile with part of styrene cinnamene to obtain a mixture A, then mixing the mixture A with a circulating material and a condensation circulating material outside a reactor in a static mixer through a metering pump so as to obtain a mixture B, and then continuously leading the mixture B to the reactor; and enabling the rest of the styrene to be pumped into a steam condenser at the top of a reaction kettle through the metering pump, to be in contact with steaming air flows of the reactor, and to be mixed with condensation steam to become a condensation circulating material, and enabling the condensation circulating material to enter the reactor through a static mixer ; (c) polymerizing a reaction mixture at 140-160 DEG C in the reactor for 1.5-2.5 hours so as to obtain an SAN copolymer; and (d) performing two-stage devolatilization in a devolatilization machine, and performing pelleting in a pelletizer, so as to obtain the high-nitrile SAN resin with narrow distribution. According to the high-nitrile SAN resin produced by the method disclosed by the invention, the percentage by mass of acrylonitrile is greater than or equal to 32%, the melt indexes of products are smaller than 6g/10min(230 DEG C, 2.16Kg), and the yellow index of the products is smaller than 12.
Owner:PETROCHINA CO LTD
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