发明名称 IMPROVED POLYTETRAMETHYLENE ETHER GLYCOL MANUFACTURING PROCESS
摘要 The present invention relates to an improved process for manufacturing polytetramethylene ether glycol. The process involves controlling the number average molecular weight of the diacetate of polytetramethylene ether glycol intermediate produced by tetrahydrofuran polymerization before methanolysis thereof to desired polytetramethylene ether glycol product.
申请公布号 US2016326316(A1) 申请公布日期 2016.11.10
申请号 US201415105781 申请日期 2014.12.19
申请人 INVISTA TECHNOLOGIES S.A.R.L. 发明人 DORAI Suri N.
分类号 C08G65/20;C08G65/30 主分类号 C08G65/20
代理机构 代理人
主权项 1. An improved process for manufacturing polytetramethylene ether glycol comprising steps of (1) polymerizing tetrahydrofuran in the presence of an acylium ion precursor at polymerization effective conditions in a polymerization reaction zone to produce a first product mixture comprising tetrahydrofuran, acylium ion precursor, acid associated with the acylium ion precursor and diacetate of polytetramethylene ether glycol; (2) feeding the first product mixture of step (1) to a first stripping zone along with additional tetrahydrofuran to produce products comprising the diacetate and tetrahydrofuran; (3) determining the number average molecular weight of the diacetate product of step (2) by the formula: Mn=((A+B)×C)/M, wherein A is the net flow rate of acylium ion precursor to step (1), B is the sum of flow rates of tetrahydrofuran to step (1) and step (2), C is the number ratio of (2× methyl acetate molecular weight) divided by the azeotropic concentration of the methyl acetate component in M by weight; and M is the flow rate of methyl acetate azeotrope product of step (5); (4) feeding the diacetate product of step (2) to a methanolysis zone along with methanol and methanolysis catalyst to produce a second product mixture comprising methyl acetate, methanol, catalyst and polytetramethylene ether glycol; (5) feeding the second product mixture of step (4) to a second stripping zone to produce products comprising methyl acetate azeotrope and polytetramethylene ether glycol; and (6) recovering the polytetramethylene ether glycol; wherein A is adjusted to control the number average molecular weight of the diacetate product of step (2) to be from about 300 to about 2300 dalton.
地址 St. Gallen CH