IP Library Granted Patent US 7,317,121
Granted Patent B2
US 7,317,121 · App. 10/941,656 · Granted Jan 8, 2008

Preparation of aliphatic oligocarbonate polyols

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Quick Facts
Patent No.
US 7,317,121
App. No.
10/941,656
Granted
Jan 8, 2008
Kind
B2
Abstract

The present invention relates to an improved process for preparing aliphatic oligocarbonate polyols by transesterifying dimethyl carbonate (DMC) with an aliphatic polyol component.

Claims (8)

1. A process for preparing oligocarbonate polyols, comprising

A) reacting dimethyl carbonate with a polyol component, in the presence of an ytterbium compound transesterification catalyst, at pressures of atmospheric pressure to 6 bar and temperatures of between 100 to 170° C.,

wherein step A) comprises n≧2 successive substeps A i ) in which i takes values of 1 to n, and in each substep A i ), a pressure 1 p i of between 3 to 6 bar is established in the reactor, a portion x i of the total amount of dimethyl carbonate is added to the liquid phase of the reaction mixture and, after a reaction time t i at a temperature T i , the methanol formed in the reaction is removed from the reaction mixture by distillation in the form of a gaseous methanol/dimethyl carbonate mixture, in the course of which the pressure is reduced, at constant temperature T i , from 1 p i to a pressure 2 p i , and in the last substep A n ), the portion x n still absent from the total amount is added and the pressure 2 p n at the end of the substep is atmospheric pressure; and

B) reducing the pressure further until a pressure of ≦100 mbar has been attained, passing an inert gas stream into the reaction mixture, such that further methanol/dimethyl carbonate mixture is distilled off in parallel, and such that the temperature of the reaction mixture does not exceed 195° C.

2. The process according to claim 1 , wherein the transesterification catalyst is ytterbium(III) acetylacetonate.

3. The process according to claim 1 , wherein the transesterification catalyst is chosen from ytterbium(III) heptadionate, ytterbium(III) acetylacetonate and ytterbium(III) chloride.

4. The process according to claim 1 , wherein the polyol component is 1,6-hexanediol.

5. The process according to claim 1 , wherein the polyol component is chosen from 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,7-heptanediol, 1,12-dodecanediol, cyclohexanedimethanol, 3-methyl-1,5-pentanediol, 2,4-diethyl-1,5-pentanediol, trimethylolpropane, pentaerythritol, bis(2-hydroxyethyl) ether, bis(6-hydroxyhexyl) ether, diols prepared by reducing dimerized unsaturated fatty acids (“dimer diols”), short-chain C 2 or C 3 polyether diols having a number-average molecular weight of <500 g/mol, short-chain C 4 polyether diols having a number-average molecular weight of <700 g/mol and mixtures thereof.

Assignments (2)
CHANGE OF NAME Recorded Mar 30, 2016
From: BAYER MATERIALSCIENCE AG
To: COVESTRO DEUTSCHLAND AG
Reel/Frame 038399/0306 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 15, 2004
From: HOFACKER, STEFFEN; WITOSSEK, HERBERT; BACKER, LOTHAR
To: BAYER MATERIALSCIENCE AG
Reel/Frame 015808/0251 →