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Catalyst for the production of polyols having lower amounts of high molecular weight tail

A catalyst, weight technology, applied in the direction of organic compound/hydride/coordination complex catalyst, physical/chemical process catalyst, catalytic reaction, etc., can solve the problem of reducing and not disclosing the amount of high molecular weight tailings

Active Publication Date: 2015-11-11
COVESTRO LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Other documents such as U.S. Patent 5,952,261 and U.S. Patent Application 2006 / 0058182 disclose the addition of cyanide-free metal salts during the catalyst precipitation step to obtain highly active catalysts effective at 30 ppm or less, but they do not Any reduction in the amount of high molecular weight tails that is disclosed or claimed to be produced during the polymerization of alkylene oxides to make polyols

Method used

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  • Catalyst for the production of polyols having lower amounts of high molecular weight tail

Examples

Experimental program
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Effect test

Embodiment 1

[0055] Preparation of DMC catalyst using potassium nitrate and polyoxypropylene glycol:

[0056] 120 g (0.88 mol) of ZnCl in 230 g of deionized water were prepared in a one-liter stirred reactor 2 and 38 g (0.513 mol) of tert-butanol in water and heated to 50° C. (solution 1). Potassium hexacyanocobaltate (8.1 g, 0.0243 mol) and potassium nitrate (5.85 g, 0.0579 mol) were dissolved in deionized water (110 g) and tert-butanol (17.2 g, 0.232 mol) in a 500 ml beaker (Solution 2 ). Solution 3 was prepared by dissolving 1000 molecular weight (mol.wt.) polyoxypropylene diol (8 grams) in deionized water (50 grams) and t-butanol (2 grams). Solution 2 was added to Solution 1 at 3.0 g / min over 42 minutes while mixing at 500 rpm. The reaction temperature was maintained at 50°C during the reaction by using an internal coil for heating or cooling. After addition, mixing was continued for 20 minutes at 500 rpm. The mixing speed was reduced and solution 3 was added, after which slow sti...

Embodiment 2

[0060] Preparation of DMC catalyst using potassium sulfate and polyoxypropylene glycol:

[0061] A solution containing 120 g (0.88 mol) of ZnCl was prepared in a one-liter stirred reactor 2 , deionized water (230 g), tert-butanol (38 g, 0.513 mol) and potassium sulfate (5.03 g, 0.029 mol) in water and heated to 50° C. (Solution 1). Potassium hexacyanocobaltate (8.1 grams, 0.0243 moles) was dissolved in deionized water (110 grams) and tert-butanol (17.2 grams, 0.232 moles) in a 500 ml beaker (Solution 2). Solution 3 was prepared by dissolving 1000 molecular weight polyoxypropylene diol (8 grams) in deionized water (50 grams) and t-butanol (2 grams). Solution 2 was added to Solution 1 at 3.0 g / min over 42 minutes while mixing at 500 rpm. The reaction temperature was maintained at 50°C during the reaction by using internal coils for heating or cooling. After addition, mixing was continued for 20 minutes at 500 rpm. The mixing speed was reduced and solution 3 was added, after ...

Embodiment 3

[0065] Preparation of DMC catalyst using potassium sulfate and 2000MW polyoxypropylene diol:

[0066] An aqueous solution containing 120 g (0.88 mol) of zinc chloride, 38 g (0.513 mol) of tert-butanol, and 5.8 g (0.033 mol) of potassium sulfate in 230 g of deionized water was prepared in a one-liter stirred reactor and heated to 50°C (Solution 1). Potassium hexacyanocobaltate (8.91 grams, 0.030 moles) was dissolved in deionized water (110 grams) and tert-butanol (18.92 grams, 0.255 moles) in a 500 ml beaker (Solution 2). Solution 3 was prepared by dissolving 2000 molecular weight polyoxypropylene diol (8 grams) in deionized water (50 grams) and t-butanol (2 grams). Solution 2 was added to Solution 1 at 3.0 g / min over 42 minutes while mixing at 500 rpm. The reaction temperature was maintained at 50°C during the reaction by using internal coils for heating or cooling. After addition, mixing was continued for 20 minutes at 500 rpm. The mixing speed was reduced and solution 3 ...

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Abstract

This invention relates to novel double metal cyanide catalysts and to a process for the production of these double metal cyanide catalysts. These DMC catalysts can be used to prepare polyoxyalkylene polyols which have low amounts of high molecular weight tail compared polyoxyalkylene polyols prepared from DMC catalysts of the prior art.

Description

Background technique [0001] The present invention relates to an improved double metal cyanide catalyst exhibiting a lower amount of high molecular weight tail, and to a process for preparing such an improved double metal cyanide catalyst. [0002] The preparation of polyoxyalkylenepolyols involves the alkoxylation of starting compounds having active hydrogen atoms with alkylene oxides in the presence of suitable catalysts. Both basic catalysts as well as DMC catalysts have been used in these alkoxylation reactions for many years. Base-catalyzed alkoxylation involves the addition of an alkylene oxide such as propylene oxide or ethylene oxide to a low molecular weight starting compound such as propylene glycol in the presence of a basic catalyst such as potassium hydroxide (KOH). or glycerol) to form polyoxyalkylene polyols. [0003] In base-catalyzed alkoxylation reactions, propylene oxide and certain other alkylene oxides undergo competing internal rearrangements, which resu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G65/10C08G65/12B01J31/12
CPCC08G65/2663B01J31/00C08G65/2606B01J27/26B01J31/068B01J31/2208B01J2231/14B01J2531/26B01J2531/845B01J31/06B01J31/16B01J31/18Y02P20/52
Inventor K·G·麦克丹尼尔G·C·库姆斯
Owner COVESTRO LLC
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