Method to Minimize the Transition Time From One Polymer Grade to Another Polymer Grade in a Polymerization Plant

    公开(公告)号:US20170240699A1

    公开(公告)日:2017-08-24

    申请号:US15510046

    申请日:2015-09-01

    IPC分类号: C08G63/78 C08G63/08

    CPC分类号: C08G63/785 C08G63/08

    摘要: The present invention relates to a method for reducing the transition time and/or the polymer waste being out of the specification during the change from a first polymer grade to a second polymer grade in a continuous polymerization process conducted in a polymerization plant, wherein the polymerization plant comprises at least one back-mixing reactor, at least one monomer and at least one processing agent selected from the group consisting of catalysts, co-catalysts, polymerization initiators, comonomers, chain-transfer agents, branching agents, solvents and arbitrary combinations of two or more of the aforementioned agents are added before and/or during the polymerization process into the at least one back-mixing reactor, wherein the concentration of one or more of the at least one added processing agent in the feed introduced into the at least one back-mixing reactor is varied as a function of time from a first value associated with the first polymer grade to a final value associated with the second polymer grade, —the first polymer grade and the second polymer grade are one or more parameters related to the molecular weight of the polymer to be produced and/or one or more parameters related to the composition of the polymer to be produced and/or one or more parameters related to the structure of the polymer to be produced and/or one or more parameters related to the amount of the polymer to be produced, wherein during the variation of the concentration of the at least one added processing agent from the first value to the final value one or more intermediate values are adjusted, wherein at least one, preferably the majority and more preferably all of the one or more intermediate values are closer to the final value than to the first value, wherein the absolute difference between the at least one, preferably each of the majority and more preferably each of all of the one or more intermediate values from the first value is greater than the absolute difference between the final and the first value, wherein the one or more intermediate values are maintained for a time which is calculated on the basis of only residence time in the at least one back-mixing reactor and steady-state correlations between input and output of the reactor and/or of the polymerization plant, and wherein the method is performed without performing dynamic modelling.

    LACTIDE BLOCK COPOLYMER AND METHOD OF PREPARATION

    公开(公告)号:US20170240696A1

    公开(公告)日:2017-08-24

    申请号:US15504219

    申请日:2015-08-18

    申请人: PURAC BIOCHEM BV

    IPC分类号: C08G63/08 C08G63/78

    CPC分类号: C08G63/08 C08G63/78

    摘要: A method for producing a lactide block copolymer, to a lactide block copolymer and to an article including the lactide block copolymer. In particular, the instant invention relates to an improved lactide block copolymer which may be obtained by providing a polymer of a first lactide monomer including a residual amount of the first monomer, adding and polymerizing a first amount of a second monomer of opposite chirality and subsequently adding and polymerizing a second amount of the second monomer. The resulting lactide block copolymer generally has a high melting point (e.g. from 190 to 250° C.).

    PRODUCTION SYSTEM/PRODUCTION PROCESS FOR ACRYLIC ACID AND PRECURSORS THEREOF
    68.
    发明申请
    PRODUCTION SYSTEM/PRODUCTION PROCESS FOR ACRYLIC ACID AND PRECURSORS THEREOF 审中-公开
    丙烯酸及其前体的生产系统/生产工艺

    公开(公告)号:US20170029352A1

    公开(公告)日:2017-02-02

    申请号:US15223178

    申请日:2016-07-29

    摘要: Provided herein are systems, and methods of using such systems, for producing acrylic acid from ethylene oxide and carbon monoxide on an industrial scale. The production system/production process has various unit operations, including, for example, a β-propiolactone production system/production process configured to produce β-propiolactone from ethylene oxide and carbon monoxide; a polypropiolactone production system/production process configured to produce polypropiolactone from β-propiolactone; and a glacial acrylic acid production system/production process configured to produce acrylic acid with a high purity by thermolysis of polypropiolactone.

    摘要翻译: 本文提供了系统和使用这种系统的方法,用于在工业规模上从环氧乙烷和一氧化碳制备丙烯酸。 生产系统/生产方法具有各种单元操作,包括例如由环氧乙烷和一氧化碳制备β-丙内酯的β-丙内酯生产系统/生产方法; 一种配制成从β-丙内酯生产聚丙内酯的聚丙内酯生产系统/制备方法; 以及通过热聚丙酸内酯制造具有高纯度的丙烯酸的冰丙烯酸生产系统/生产方法。

    Process for manufacturing polyethylene terephthalate
    70.
    发明授权
    Process for manufacturing polyethylene terephthalate 有权
    聚对苯二甲酸乙二醇酯的制造方法

    公开(公告)号:US09534080B2

    公开(公告)日:2017-01-03

    申请号:US14655793

    申请日:2013-11-30

    摘要: The invention relates to a process for producing a polyester resin, said process comprises the steps of (i) providing a mixture of terephthalic acid, monoethylene glycol, a polycondensation catalyst which contains antimony, a phosphorous containing stabilizer comprising a compound of the formula (I) and optionally a colour correction additive containing cobalt ions; (ii heating said mixture to a temperature of 220 to 270° C. to provide bis-hydroxyethylterephthalic acid ester; and (iii) performing polycondensation of said bis-hydroxyethylterephthalic acid ester at a temperature of between 280 and 310° C. at reduced pressure.

    摘要翻译: 本发明涉及一种生产聚酯树脂的方法,所述方法包括以下步骤:(i)提供对苯二甲酸,一乙二醇,含锑的缩聚催化剂的混合物,含磷稳定剂,其包含式(I )和任选的含有钴离子的颜色校正添加剂; (ii)将所述混合物加热至220至270℃的温度以提供双 - 羟乙基对苯二甲酸酯; 和(iii)在减压下在280-310℃的温度下进行所述双羟乙基对苯二甲酸酯的缩聚。