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    • 4. 发明授权
    • Process for the in-situ production of polyol blends, the in-situ produced polyol blends, and their use in the production of viscoelastic foam
    • 多元醇共混物的原位生产方法,原位制备的多元醇共混物及其在生产粘弹性泡沫中的应用
    • US06491846B1
    • 2002-12-10
    • US09886510
    • 2001-06-21
    • Jack R. Reese, IIStanley L. Hager
    • Jack R. Reese, IIStanley L. Hager
    • C08G1814
    • C08G18/283C08G18/4866C08G65/2663C08G65/2696C08G2101/0008C08G2101/005C08G2101/0083
    • This invention relates to a process for the in-situ production of a blend of a polyether monol and a polyether polyol. This process comprises introducing a monol (Si) and a double metal cyanide (DMC) catalyst into a reaction vessel, feeding an epoxide mixture into the vessel and allowing the epoxide to react with the initial starter and continuing to polymerize by feeding epoxide until the equivalent weight of the monol reaches the desired level, then continuously adding a polyfunctional starter (Sc) to the reaction vessel while continuing to feed an epoxide mixture, completing addition of the starter, and allowing the mixture to continue to polymerize until the resultant blend of polyether monol and polyether polyol has an average equivalent weight of from about 350 to about 750, and an average functionality of from about 2 to about 4. In-situ polymerized blends of a polyether monol and a polyether polyol are also part of the present invention. The present invention also relates to a process for the production of viscoelastic foams. This process comprises reacting a polyisocyanate component with an isocyanate-reactive component, in the presence of additives, wherein the isocyanate-reactive component comprises at least 50% by weight of the in-situ polymerized blend of a polyether monol and a polyether polyol as described above.
    • 本发明涉及一种原位生产聚醚单醇和聚醚多元醇共混物的方法。 该方法包括将单醇(Si)和双金属氰化物(DMC)催化剂引入反应容器中,将环氧化物混合物进料到容器中,并使环氧化物与初始起始物反应,并通过进料环氧化物继续聚合直到等效 一元醇的重量达到所需的水平,然后连续地向反应容器中加入多官能起始物(Sc),同时继续加入环氧化物混合物,完成起始物的添加,并使混合物继续聚合,直到得到的聚醚共混物 单醇和聚醚多元醇的平均当量为约350至约750,平均官能度为约2至约4.聚醚一元醇和聚醚多元醇的原位聚合共混物也是本发明的一部分。 本发明还涉及制备粘弹性泡沫的方法。 该方法包括在添加剂存在下使多异氰酸酯组分与异氰酸酯反应性组分反应,其中异氰酸酯反应性组分包含如所述的至少50重量%的聚醚一元醇和聚醚多元醇的原位聚合共混物 以上。
    • 6. 发明授权
    • Process for the production of polyoxyalkylene containing polyols from phenol condensation products
    • 用于由苯酚缩合产物生产含聚氧化烯的多元醇的方法
    • US07538162B2
    • 2009-05-26
    • US11473686
    • 2006-06-23
    • Karl W. HaiderStanley L. HagerJack R. Reese, II
    • Karl W. HaiderStanley L. HagerJack R. Reese, II
    • C08L71/10
    • C08G65/2663
    • This invention relates to a one-stage process for the production of polyoxyalkylene containing polyols having equivalent weights of about 150 to about 6000 and functionalities of about 2 to 8. The process comprises (1) mixing (a) an organic compound having a hydroxyl functionality of about 2 to about 8 and an equivalent weight of about 35 to about 575, with (b) a hydroxyl functional compound having an equivalent weight of about 100 to about 6000 and a functionality of about 2 to 8; and (2) alkoxylating the mixture with (c) one or more alkylene oxides, in the presence of (d) one or more double metal cyanide catalysts. Suitable compounds to be used as (a) the organic compound having a hydroxyl functionality of about 2 to about 8 and an equivalent weight of about 35 to about 575 in the present invention include bisphenol-A, Bisphenol TMC, tetrabromobisphenol A, and novolak phenolic resins.
    • 本发明涉及用于生产具有约150至约6000当量和约2至8的官能度的含聚氧化烯的多元醇的一步法。该方法包括(1)将(a)具有羟基官能度的有机化合物 约2至约8,当量为约35至约575,和(b)当量为约100至约6000,官能度为约2至8的羟基官能化合物; 和(2)在(d)一种或多种双金属氰化物催化剂的存在下,使(c)一种或多种烯化氧烷化该混合物。 用作本发明中(a)羟基官能度为约2至约8,当量约35至约575的有机化合物的合适化合物包括双酚A,双酚TMC,四溴双酚A和酚醛清漆酚 树脂。