Production process for diglycidyl-capped polyalkylene glycols with in-situ removal of 1,4-dioxane
US-2018319934-A1 · Nov 8, 2018 · US
US2016289381A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016289381-A1 |
| Application number | US-201415035422-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 18, 2014 |
| Priority date | Nov 22, 2013 |
| Publication date | Oct 6, 2016 |
| Grant date | — |
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The present invention concerns a catalyst formulation comprising: (a) a Zn catalyst comprising a Zn compound having alcoholate ligand(s) derived from one or more polyols, and (b) a catalyst additive comprising a metal compound (i) having alcoholate ligand(s) derived from one or monohydric alcohol wherein the metal is selected from: (I) first row transition metals excluding Zn, preferably Sc, Ti, V, Cr, Mn, Ni, and Co, more preferably Ti, (II) second row transition metals, preferably Y and Zr, more preferably Zr, and (III) combinations of at least two metals selected from (I) and (II). The present invention also relates to a process for polymerizing an epoxide monomer, preferably ethylene oxide, comprising carrying out the process in the presence of the catalyst formulation.
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1 . A catalyst formulation comprising: (a) a Zn catalyst comprising a Zn compound having alcoholate ligand(s) derived from one or more polyols, and (b) a catalyst additive comprising a metal compound (i) having alcoholate ligand(s) derived from a monohydric alcohol wherein the metal is selected from: (I) first row transition metals excluding Zn, (II) second row transition metals, and (III) combinations of at least two metals selected from (I) and (II). 2 . The catalyst formulation of claim 1 wherein the Zn compound of the Zn catalyst (a) is selected from: (a1) a Zn alcoholate of one or more polyols, and (a2) a heteroleptic Zn alcoholate of one or more polyols and one or more monohydric alcohols and/or water. 3 . The catalyst formulation of claim 2 wherein the Zn catalyst (a) comprises a Zn alcoholate (a1) of one or more polyols and a Zn alcoholate (a3) of one or more monohydric alcohols. 4 . The catalyst formulation of claim 1 wherein the Zn catalyst (a) comprises a Zn compound having alcoholate ligand(s) derived from one or more diols. 5 . The catalyst formulation of any one of claim 2 wherein the Zn compound of the Zn catalyst (a) is a heteroleptic Zn alcoholate (a2) of one ore more polyols and one or more monohydric alcohols selected from monohydric aliphatic alcohols including monohydric halosubstituted aliphatic alcohols. 6 . The catalyst formulation of claim 5 wherein the Zn compound of the Zn catalyst (a) is a heteroleptic Zn alcoholate (a2) of 1,4-butanediol and ethanol. 7 . The catalyst formulation of claim 1 wherein the catalyst additive (b) comprises a metal compound (i) having alcoholate ligand(s) derived from one or monohydric aliphatic, cycloaliphatic or mixed aliphatic/cycloaliphatic alcohols. 8 . The catalyst formulation of claim 1 wherein the metal compound (i) of the catalyst additive (b) is selected from: (b1) a metal alcoholate of one or more monohydric alcohols, and (b2) a heteroleptic metal complex having alcoholate ligand(s) derived from one or more monohydric alcohols and non-alcoholate ligand(s). 9 . The catalyst formulation of claim 1 wherein the catalyst additive additionally comprises (ii) a monohydric alcohol. 10 .- 12 . (canceled) 13 . A process for polymerizing an epoxide monomer comprising carrying out the process in the presence of a catalyst formulation comprising: (a) a Zn catalyst comprising a Zn compound having alcoholate ligand(s) derived from one or more polyols, and (b) a catalyst additive comprising a metal compound (i) having alcoholate ligand(s) derived from a monohydric alcohol wherein the metal is selected from: (I) first row transition metals excluding Zn, (II) second row transition metals, and (III) combinations of at least two metals selected from (I) and (II). 14 . The process of claim 13 wherein a poly(olefin oxide having a weight average molecular weight of at least 30,000 is prepared. 15 . The process of claim 13 wherein the metal compound (i) is present in an amount providing a molar ratio of metal of the metal compound (i) to Zn of the Zn catalyst (a) within the range of from 0.01:1 to 20:1. 16 . The process of claim 13 wherein a poly(ethylene oxide) is prepared. 17 . The process of claim 14 wherein a poly(ethylene oxide) is prepared.
containing organo-metallic compounds or metal hydrides · CPC title
Mixed catalyst systems, i.e. containing more than one reactive component or catalysts formed in-situ · CPC title
Metallic elements not covered by group C08G65/2648 - C08G65/2645, or compounds thereof · CPC title
characterised by the catalysts used · CPC title
Lithium · CPC title
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