Production process for diglycidyl-capped polyalkylene glycols with in-situ removal of 1,4-dioxane
US-2018319934-A1 · Nov 8, 2018 · US
US9879115B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9879115-B2 |
| Application number | US-201415035422-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 18, 2014 |
| Priority date | Nov 22, 2013 |
| Publication date | Jan 30, 2018 |
| Grant date | Jan 30, 2018 |
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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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What is claimed is: 1. 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) Ti, (II) Zr, and (III) a combination of Ti and Zr, wherein water and oxygen are excluded from the catalyst formulation and a poly(olefin oxide) having a weight average molecular weight of 30,000 to 2,000,000 is prepared. 2. The process of claim 1 wherein a poly(olefin oxide) having a weight average molecular weight of 50,000 to 2,000,000 is prepared. 3. The process of claim 1 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. 4. The process of claim 1 wherein a poly(ethylene oxide) is prepared. 5. The process of claim 2 wherein a poly(ethylene oxide) is prepared. 6. The process of claim 1 wherein a poly(ethylene oxide) is prepared which has a molecular weight of 100,000 to 2,000,000 based on viscosity determination.
containing organo-metallic compounds or metal hydrides · CPC title
characterised by the catalysts used · 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
Lithium · CPC title
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