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    • 91. 发明申请
    • Method for producing polyether alcohols
    • 聚醚醇的制造方法
    • US20070129577A1
    • 2007-06-07
    • US10578874
    • 2004-11-06
    • Thomas OstrowskiRaimund RuppelEva BaumKatherine Harre
    • Thomas OstrowskiRaimund RuppelEva BaumKatherine Harre
    • C07C41/03
    • C08G65/2663C08G18/4866C08G65/2696
    • The invention relates to a process for the continuous preparation of polyether alcohols by reaction of alkylene oxides with H-functional starter substances in the presence of DMC catalysts, which comprises, at the beginning of the process a) firstly placing initial charge material and DMC catalyst in a reactor, b) metering in alkylene oxide so that the metering rate which is maintained for continuous operation of the reactor is reached in a time of from 100 to 3000 seconds, c) metering in starter substance during or after step b) so that the metering rate which is maintained for continuous operation of the reactor is reached in a time of from 5 to 500 seconds, d) after the fill level in the reactor which is desired for continuous operation of the reactor has been reached, taking product off continuously from the reactor while at the same time metering in starter substance and alkylene oxides in such an amount that the fill level in the reactor remains constant and metering in DMC catalyst so that the catalyst concentration necessary for continuous operation of the reactor is maintained in the reactor.
    • 本发明涉及一种通过在DMC催化剂存在下使烯化氧与H官能起始物质反应来连续制备聚醚醇的方法,该方法在方法开始时包括:a)首先将初始的电荷材料和DMC催化剂 在反应器中,b)在环氧烷中计量,使得在100至3000秒的时间内达到维持反应器连续操作的计量速率,c)在步骤b)期间或之后计量起始物质,使得 在5至500秒的时间内达到维持反应器连续运行的计量率,d)在达到反应器连续运行所需反应器的填充量后,连续停止生产 同时在起始物质和环氧烷中同时计量反应器中的填充水平保持恒定并在DMC催化剂中计量的量 使得在反应器中保持连续操作反应器所需的催化剂浓度。
    • 93. 发明申请
    • Production processes for alkylene oxide addition product and its derivatives
    • 烯化氧加成产物及其衍生物的生产方法
    • US20050080298A1
    • 2005-04-14
    • US10500554
    • 2003-05-02
    • Toru InaokaYoshiyuki OndaHiromichi TanakaTsuyoshi Hirata
    • Toru InaokaYoshiyuki OndaHiromichi TanakaTsuyoshi Hirata
    • C08F299/02C08G65/26C08G65/28C08G65/332C07C67/26C08G59/14
    • C08G65/2609C08G65/2696C08G65/3322
    • The present invention provides: a production process for an alkylene oxide addition product, by which a high-molecular alkylene oxide addition product can be obtained with ordinary production facilities while the formation of by-products is suppressed; and production processes for derivatives from the alkylene oxide addition product. The present invention production process for an alkylene oxide addition product comprises the step of carrying out an addition reaction of an alkylene oxide to a hydroxyl-group-containing saturated compound in order to obtain the alkylene oxide addition product; with the production process being characterized by further comprising: the initial step of causing the alkylene oxide to add to the hydroxyl-group-containing saturated compound in an amount of not larger than 20 mols on average of the alkylene oxide per 1 mol of the hydroxyl-group-containing saturated compound to thereby obtain an alkylene oxide low-mol-addition product; and the molar-degree-of-polyaddition-adjusting step of causing the alkylene oxide to further add to the alkylene oxide low-mol-addition product as obtained in the initial step; wherein a portion of the entirety of the alkylene oxide low-mol-addition product as obtained in the initial step is used in the molar-degree-of-polyaddition-adjusting step.
    • 本发明提供:一种环氧烷加成物的制造方法,通过该方法可以获得具有普通生产设备的高分子量烯化氧加成产物,同时抑制副产物的形成; 以及来自烯化氧加成产物的衍生物的制备方法。 本发明的烯化氧加成产物的制备方法包括进行烯化氧与含羟基的饱和化合物的加成反应以获得环氧烷烃加成产物的步骤; 其制备方法的特征还在于:使每1摩尔羟基的烯化氧的平均相对于含有羟基的饱和化合物不少于20摩尔的环氧烷加成的初始步骤 含有饱和化合物,得到环氧烷低摩尔加成产物; 和加成摩尔加聚度调整步骤,使得氧化烯进一步添加到初始步骤中获得的环氧烷低摩尔加成产物; 其中在初始步骤中获得的全部烯化氧低摩尔加成产物的一部分用于加聚度加聚步骤。
    • 95. 发明授权
    • Activated starter mixtures and the processes related thereto
    • 活化起动​​混合物及其相关工艺
    • US06835801B2
    • 2004-12-28
    • US10199916
    • 2002-07-19
    • John E. Hayes
    • John E. Hayes
    • C08G6510
    • C08G65/2696C08G18/4866C08G65/2609C08G65/2663
    • The present invention is directed to an activated starter mixture which can be used to prepare polyoxyalkylene polyols. The present invention is also directed to a process for preparing an activated starter mixture, particularly, to a process for preparing an activated starter mixture which is composed of a low molecular weight starter compound. The present invention is also directed to a batch or semi-batch process for the polyaddition of an alkylene oxide on to an activated starter mixture, particularly, on to an activated starter mixture which is composed of a low molecular weight starter compound. The present invention provides an activated starter mixture, particularly, an activated starter mixture which is composed of a low molecular weight starter compound, which rapidly initiates polymerization. The present invention can eliminate the need to synthesize costly high molecular weight starter compounds by KOH catalysis in a separate, dedicated reactor.
    • 本发明涉及可用于制备聚氧化烯多元醇的活化起始混合物。 本发明还涉及一种制备活化起始混合物的方法,特别是制备由低分子量起始化合物组成的活化起始混合物的方法。 本发明还涉及用于将烯化氧加成到活化起始混合物上的批次或半间歇方法,特别是涉及由低分子量起始化合物组成的活化起始混合物。本发明 提供活化的起始混合物,特别是由低分子量起始化合物组成的活化起始混合物,其迅速引发聚合。 本发明可以消除在单独的专用反应器中通过KOH催化合成昂贵的高分子量起始物化合物的需要。
    • 97. 发明授权
    • Methods for producing a polyol and a polymer dispersed polyol
    • 制备多元醇和聚合物分散多元醇的方法
    • US06815467B2
    • 2004-11-09
    • US10197528
    • 2002-07-18
    • Yoshinori ToyotaAkio HorieHiroshi WadaKayoko SugiyamaEtsuko Akagi
    • Yoshinori ToyotaAkio HorieHiroshi WadaKayoko SugiyamaEtsuko Akagi
    • C08G1828
    • C08G65/2696C08G18/0857C08G18/4063C08G18/4072C08G18/4866C08G18/657C08G18/7607C08G65/02C08G65/2663C08G2101/0008C08G2101/005C08G2101/0083C08J2205/06
    • A method for producing a polyoxyalkylene polyol which comprises subjecting propylene oxide and ethylene oxide to ring-opening addition polymerization with an initiator in the presence of a catalyst, wherein the polyoxyalkylene polyol is a polyoxyalkylene polyol obtained by subjecting propylene oxide to ring-opening addition polymerization with an initiator in the presence of a double metal cyanide complex catalyst to form an oxypropylene block chain, subjecting ethylene oxide and propylene oxide to ring-opening addition polymerization randomly to form an oxyalkylene random chain, changing the catalyst and subjecting ethylene oxide to ring-opening addition polymerization in the presence of an alkali metal catalyst to form an oxyethylene block chain, and the polyoxyalkylene polyol is a polyoxyalkylene polyol having a hydroxyl value of from 5 to 56 mgKOH/g, a proportion of an initiator residue of at most 25 mass %, a proportion of the oxypropylene block chain of from 5 to 50 mass %, a total oxyethylene group content of from 5 to 60 mass %, and a ratio of primary hydroxyl groups among terminal hydroxyl groups of at least 60 mol %.
    • 一种聚氧化烯多元醇的制造方法,其特征在于,在催化剂的存在下,使用环氧丙烷与环氧乙烷进行开环加成聚合,其中,所述聚氧化烯多元醇是通过使环氧丙烷进行开环加成聚合得到的聚氧化烯多元醇 在双金属氰化物配合物催化剂的存在下引发剂形成氧化丙烯嵌段链,使环氧乙烷和环氧丙烷随机开环加成聚合形成氧化烯无规链,改变催化剂并使环氧乙烷进行环 - 在碱金属催化剂存在下开环加成聚合形成氧乙烯嵌段链,聚氧化烯多元醇为羟值为5〜56mgKOH / g的聚氧化烯多元醇,引发剂残基的比例为25质量%以下 %,氧丙烯嵌段链的比例为5〜50质量%,总计 氧乙烯基含量为5〜60质量%,末端羟基的伯羟基比例为60摩尔%以上。