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    • 2. 发明申请
    • High water content tolerant process for the production of polyethers
    • 用于生产聚醚的高耐水含量方法
    • US20080021191A1
    • 2008-01-24
    • US11490303
    • 2006-07-20
    • Jack R. ReeseEdward P. BrowneJose F. Pazos
    • Jack R. ReeseEdward P. BrowneJose F. Pazos
    • C08G18/00
    • C08G18/4866C08G65/2663C08G65/2696
    • The present invention provides a process for the production of a polyether involving establishing oxyalkylation conditions in an oxyalkylation reactor in the presence of from about 5 ppm to about 1,000 ppm, based on the final polyether weight, of a double metal cyanide (DMC) catalyst, continuously introducing into the reactor at least one alkylene oxide and a low molecular weight starter having a number average molecular weight of less than about 300 Daltons (Da) containing from about 200 ppm to about 5,000 ppm water and acidified with from about 10 ppm to about 2,000 ppm of at least one of an inorganic protic mineral acid and an organic acid, and recovering a polyether product having a number average molecular weight of from about 200 Da to about 4,000 Da, wherein the ppm (parts per million) of water and acid are based on the weight of the low molecular weight starter. The inventive process may allow for the use of low molecular weight starters containing higher levels of water at lower DMC catalyst levels than current processes.
    • 本发明提供了一种制备聚醚的方法,包括在烷氧基化反应器中,在最终的聚醚重量为约5ppm至约1,000ppm的情况下,制备双金属氰化物(DMC)催化剂, 连续向反应器中引入至少一种数均分子量小于约300道尔顿(Da)的环氧烷和低分子量起始物,其含有约200ppm至约5,000ppm的水并用约10ppm至约 2,000ppm的无机质子性无机酸和有机酸中的至少一种,并回收数均分子量为约200Da至约4,000Da的聚醚产物,其中ppm(ppm / ppm)的水和酸 基于低分子量起始物的重量。 本发明的方法可以允许使用含有比当前方法更低的DMC催化剂水平的较高水平的水的低分子量起动器。
    • 9. 发明申请
    • PROCESS FOR THE PRODUCTION OF LOW MOLECULAR WEIGHT IMPACT POLYETHERS
    • 生产低分子量重力聚合物的方法
    • US20130345476A1
    • 2013-12-26
    • US13528909
    • 2012-06-21
    • Jack R. Reese
    • Jack R. Reese
    • C07C41/02C07C41/03
    • C07C41/03C08G65/2609C08G65/2663C08G65/2696C08G65/30C07C43/11
    • This invention relates to an improved continuous process for the production of low molecular weight polyoxyalkylene polyether polyols. These polyoxyalkylene polyether polyols have a hydroxyl content of from about 3.4 to about 12.1% by weight, and may also be characterized as having an OH number of from about 112 to about 400. The process comprises establishing oxyalkylation conditions in a continuous reactor in the presence of a DMC catalyst; continuously introducing alkylene oxide and a low molecular weight starter into the continuous reactor; recovering a partially oxyalkylated polyether polyol from the reactor; and allowing the recovered partially oxyalkylated polyether polyol to further reactor until the unreacted alkylene oxide content of the mixture is reduced to 0.001% or less by weight.
    • 本发明涉及用于生产低分子量聚氧化烯聚醚多元醇的改进的连续方法。 这些聚氧化烯聚醚多元醇具有约3.4至约12.1重量%的羟基含量,并且还可以表征为具有约112至约400的OH值。该方法包括在存在下在连续反应器中建立烷氧基化条件 的DMC催化剂; 将环氧烷和低分子量起始剂连续引入连续反应器中; 从反应器中回收部分烷氧基化聚醚多元醇; 并将回收的部分烷氧基化聚醚多元醇进一步反应,直到混合物的未反应的烯化氧含量降低至0.001重量%以下。