公开(公告)号：US20110009675A1

公开(公告)日：2011-01-13

申请号：US12745648

申请日：2008-12-08

申请人： Max Tirtowidjojo ,  Edward D. Daugs

发明人： Max Tirtowidjojo ,  Edward D. Daugs

IPC分类号： C07C41/09

CPC分类号： C07C41/03 ,  Y02P20/582 ,  C07C43/23

摘要： Phenolic glycol ethers, e.g., ethylene glycol phenyl ether, are prepared by a continuous, nonaqueous process comprising the steps of (A) contacting under isothermal reactive conditions in a first reactor or reaction zone an alkylene oxide, e.g., ethylene oxide, with (i) a stoichiometric molar excess of a phenolic compound, e.g., phenol, and (ii) a catalytic amount of a base, e.g., sodium hydroxide, homogeneously dispersed throughout the phenolic compound, to form a first intermediate phenolic glycol ether product, (Bj transferring the first intermediate phenolic glycol ether product to a second reactor or reaction zone, and (C) subjecting the first intermediate phenolic glycol ether product to adiabatic reactive conditions in the second reactor or reaction zone to form a second intermediate phenolic glycol ether product comprising phenolic glycol ether, unreacted phenolic compound, catalyst, water and byproduct glycols. In addition, the mono-/di-product weight ratio can be adjusted by increasing or decreasing the amount of base catalyst employed.

摘要翻译： 酚醛二醇醚，例如乙二醇苯基醚，通过连续的非水性方法制备，包括以下步骤：（A）在等温反应条件下在第一反应器或反应区中接触环氧烷，例如环氧乙烷与（i ）化学计量摩尔过量的酚类化合物，例如苯酚，和（ii）催化量的碱，例如均匀分散在整个酚类化合物中的氢氧化钠，形成第一中间体酚二醇醚产物（Bj转移 将第一中间体酚二醇醚产物加入到第二反应器或反应区中，和（C）使第一中间体酚二醇醚产物在第二反应器或反应区中进行绝热反应条件以形成包含酚二醇的第二中间体酚二醇醚产物 醚，未反应的酚类化合物，催化剂，水和副产物二醇，另外，单/二产物重量比可以通过 增加或减少所用的碱催化剂的量。

公开(公告)号：US08558029B2

公开(公告)日：2013-10-15

申请号：US12745648

申请日：2008-12-08

申请人： Max Tirtowidjojo ,  Edward D. Daugs

发明人： Max Tirtowidjojo ,  Edward D. Daugs

IPC分类号： C07C43/23

CPC分类号： C07C41/03 ,  Y02P20/582 ,  C07C43/23

摘要： Phenolic glycol ethers, e.g., ethylene glycol phenyl ether, are prepared by a continuous, nonaqueous process comprising the steps of (A) contacting under isothermal reactive conditions in a first reactor or reaction zone an alkylene oxide, e.g., ethylene oxide, with (i) a stoichiometric molar excess of a phenolic compound, e.g., phenol, and (ii) a catalytic amount of a base, e.g., sodium hydroxide, homogeneously dispersed throughout the phenolic compound, to form a first intermediate phenolic glycol ether product, (Bj transferring the first intermediate phenolic glycol ether product to a second reactor or reaction zone, and (C) subjecting the first intermediate phenolic glycol ether product to adiabatic reactive conditions in the second reactor or reaction zone to form a second intermediate phenolic glycol ether product comprising phenolic glycol ether, unreacted phenolic compound, catalyst, water and byproduct glycols. In addition, the mono-/di-product weight ratio can be adjusted by increasing or decreasing the amount of base catalyst employed.

摘要翻译： 酚醛二醇醚，例如乙二醇苯基醚，通过连续的非水性方法制备，包括以下步骤：（A）在等温反应条件下在第一反应器或反应区中接触环氧烷，例如环氧乙烷与（i ）化学计量摩尔过量的酚类化合物，例如苯酚，和（ii）催化量的碱，例如均匀分散在整个酚类化合物中的氢氧化钠，形成第一中间体酚二醇醚产物（Bj转移 将第一中间体酚二醇醚产物加入到第二反应器或反应区中，和（C）使第一中间体酚二醇醚产物在第二反应器或反应区中进行绝热反应条件以形成包含酚二醇的第二中间体酚二醇醚产物 醚，未反应的酚类化合物，催化剂，水和副产物二醇，另外，单/二产物重量比可以通过 增加或减少所用的碱催化剂的量。

公开(公告)号：US20140088329A1

公开(公告)日：2014-03-27

申请号：US13575266

申请日：2012-05-30

申请人： Max Tirtowidjojo ,  William J. Kruper, JR. ,  Kurt F. Hirsekorn ,  Debashis Chakraborty

发明人： Max Tirtowidjojo ,  William J. Kruper, JR. ,  Kurt F. Hirsekorn ,  Debashis Chakraborty

IPC分类号： C07C21/073 ,  C07C17/26

CPC分类号： C07C21/073 ,  C07C17/26 ,  C07C17/269

摘要： Processes for the production of chlorinated and/or fluonnated propenes provide good product yield with advantageous impurity profiles in the crude product. Advantageously, the processes may be conducted at lower temperatures than 600° C., or less than 500° C., so that energy savings are provided, and/or at higher pressures so that high throughputs may also be realized. The use of catalysts or initiators may provide additional enhancements to conversion rates and selectivity, as may adjustments to the molar ratio of the reactants.

摘要翻译： 用于生产氯化和/或氟化丙烯的方法提供良好的产物产率，并且在粗产物中具有有利的杂质分布。 有利地，该方法可以在比600℃或低于500℃的较低温度下进行，以便提供能量节省和/或在更高的压力下进行，从而也可以实现高通量。 催化剂或引发剂的使用可以提供对转化率和选择性的额外增强，如可以调节反应物的摩尔比。