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A method for refining polyether polyol using bipolar membrane electrodialysis system

A bipolar membrane electrodialysis and polyether polyol technology is applied in the field of polyether polyol to achieve the effects of short production cycle, green and simple process, and reduced production cost

Active Publication Date: 2022-07-12
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

So far, there has been no report on the use of bipolar membrane electrodialysis system for refining polyether polyols

Method used

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  • A method for refining polyether polyol using bipolar membrane electrodialysis system
  • A method for refining polyether polyol using bipolar membrane electrodialysis system
  • A method for refining polyether polyol using bipolar membrane electrodialysis system

Examples

Experimental program
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Effect test

Embodiment 1

[0037] (1) Surface modification of the cation exchange membrane by dipping method.

[0038] The first step, pretreatment: take a 600*1200mm PVA cation exchange membrane, wash the membrane surface impurities with deionized water, and then soak it in absolute ethanol for 2 hours before use.

[0039] The second step is to prepare the immersion solution: stir 50ml of butyl titanate and 50ml of absolute ethanol with a magnetic stirrer for 1 hour, and then slowly and continuously drop in (45min added) with 50ml of absolute ethanol, 5ml of water and 2.5ml of concentrated hydrochloric acid. The resulting mixture was continued to stir for 1 h before use.

[0040] The third step, dip coating: the cation exchange membrane of the first step is immersed in the dipping solution of the second step, taken out after 4 hours, heat-treated at 90°C for 12 hours, and washed with water for use.

[0041] (2) Build as image 3 The bipolar membrane electrodialysis device shown, the anode and cathode...

Embodiment 2

[0045] (1) Surface modification of the cation exchange membrane by dipping method.

[0046] The first step, pretreatment: take a 600*1200mm PVA cation exchange membrane, wash the membrane surface impurities with deionized water, and then soak it in absolute ethanol for 2 hours before use.

[0047] The second step is to prepare the immersion solution: stir 15ml of butyl titanate and 10ml of absolute ethanol with a magnetic stirrer for 1 hour, and then slowly and continuously drop in (35min added), which is made up of 50ml of absolute ethanol, 1.5ml of water and 10ml of acetic acid The mixture was continued to stir for 1 h before use.

[0048] The third step, dipping coating: the cation exchange membrane of the first step is immersed in the dipping solution of the second step, taken out after 2 hours, heat treated at 90°C for 24 hours, washed with water for use.

[0049] (2) Build as image 3 The bipolar membrane electrodialysis device shown is different from Example 1 in that...

Embodiment 3

[0053] (1) Surface modification of the cation exchange membrane by dipping method.

[0054] The first step, pretreatment: take a 600*1200mm PVA cation exchange membrane, wash the membrane surface impurities with deionized water, and then soak it in absolute ethanol for 2 hours before use.

[0055] The second step is to prepare the immersion solution: stir 15ml of isopropyl titanate and 15ml of absolute ethanol with a magnetic stirrer for 1 hour, then slowly and continuously drop in (60min added), which is made up of 60ml of absolute ethanol, 3ml of water and 10ml of acetic acid The mixture was continued to stir for 1 h before use.

[0056] The third step, dipping coating: the cation exchange membrane of the first step is immersed in the dipping solution of the second step, taken out after 3 hours, heat treated at 100°C for 16 hours, and washed with water for use.

[0057] (2) Build as image 3 The bipolar membrane electrodialysis device shown differs from Example 1 in that t...

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Abstract

The invention discloses a method for using a modified cation exchange membrane to construct a bipolar membrane electrodialysis system to purify polyether polyol. Alkali resistance, and then use the modified cation exchange membrane to build a bipolar membrane electrodialysis system, mix the crude polyether polyol synthesized by alkali catalysis with water and introduce it into the system, and the alkali (earth) metal ions in the crude product are permeated and modified The cation exchange membrane and the hydroxide ions generated by the hydrolysis of the bipolar membrane are used in the alkali chamber to form alkali solution for recycling, and the hydrogen ions generated by the bipolar membrane hydrolysis enter the material chamber to reduce the alkali value of the product without consuming neutralizing acid. The modified cation exchange membrane of the invention has good hydrophilicity and strong alkali resistance, is suitable for treating polyether polyol system, reduces the cost of the refining process of polyether polyol, and has good application prospect.

Description

technical field [0001] The invention relates to a method for purifying polyether polyol by using a modified cation exchange membrane to construct a bipolar membrane electrodialysis system, and belongs to the field of polyether polyol. Background technique [0002] Polyether polyol is an important raw material for the production of polyurethane materials, and is widely used in many fields such as defoamers, demulsifiers, additives, and cleaning agents. Polyether polyols usually use alkali (earth) metal hydroxides as catalysts, and are formed by ring-opening polymerization of compounds with active hydrogen atoms as initiators and alkylene oxides. The crude polyether polyol produced by polymerization contains alkali (earth) metal catalysts, and alkali (earth) metal ions will adversely affect the performance of downstream products, so it needs to be purified to remove alkali (earth) metal ions. [0003] At present, the main industrial refining process of polyether polyol is to ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D61/44B01D61/48C08G65/30
CPCB01D61/445B01D61/485C08G65/30Y02P20/10
Inventor 李传亮黎源秦承群刘斌石正阳隋美玉殷玲吕树卫姜明
Owner WANHUA CHEM GRP CO LTD