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Method for preparing polymeric blend membrane by nonsolvent induced gel phase separation method

A gel phase separation method and polymer technology, applied in semi-permeable membrane separation, chemical instruments and methods, membrane technology, etc., can solve problems such as difficult to achieve high performance and anti-pollution performance, and achieve excellent separation performance and mechanical properties , Excellent permanent hydrophilicity, high-purity water flux effect

Inactive Publication Date: 2018-09-14
TIANJIN POLYTECHNIC UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In short, it is difficult to achieve high performance and anti-fouling properties of membrane materials prepared by adding non-solvent additives to the casting solution.

Method used

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  • Method for preparing polymeric blend membrane by nonsolvent induced gel phase separation method
  • Method for preparing polymeric blend membrane by nonsolvent induced gel phase separation method
  • Method for preparing polymeric blend membrane by nonsolvent induced gel phase separation method

Examples

Experimental program
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Effect test

Embodiment 1

[0021] The method for preparing the polymer blend membrane by the non-solvent-induced gel phase separation method is as follows: Weigh 7.56g polyethersulfone, 1.44g sulfonated polysulfone, 12g polyethylene glycol (molecular weight 1kDa), dissolve in 41g DMAc , and then 4.5 g of non-solvent water was added thereto, and then mechanically stirred for 8 hours under the condition of 70° C. water bath to obtain a homogeneous solution, and left to defoam under the condition of 70° C. water bath. Then scrape the casting solution on a clean glass plate, lower it to room temperature, and then immerse it in the coagulation bath-water to solidify to form a film. The results show that the cross-section of the obtained blend membrane is an asymmetric gradient open-pore sponge structure, and its pure water flux is 1158L / m 2 h, the rejection rate of bovine serum albumin (BSA) is 95.5%, and the breaking strength reaches 3.5MPa.

Embodiment 2

[0023] The method for preparing the polymer blend membrane by the non-solvent-induced gel phase separation method is as follows: Weigh 8.4g polyethersulfone, 1.6g sulfonated polyethersulfone, 10g polyethylene glycol (molecular weight 30kDa), dissolve in 40g DMAc 4 g of non-solvent ethanol (95v / v%) was added thereto, then mechanically stirred under 70°C water bath conditions for 8 hours, and after obtaining a homogeneous solution, stand for defoaming under 70°C water bath conditions. Then scrape the casting solution on a clean glass plate, after cooling down to room temperature, then immerse it in the coagulation bath-water to solidify to form a film. The results show that the cross-section of the blend membrane obtained under this condition is an asymmetric gradient open-pore sponge structure, and its pure water flux is 820L / m 2 h, the rejection rate of BSA is 98.7%, and the mechanical strength reaches 4.2MPa.

Embodiment 3

[0025] The method for preparing polymer blend membrane by non-solvent-induced gel phase separation method is as follows: Weigh 10.08g polysulfone, 1.92g sulfonated polyether ether ketone, 6.0g PVP (molecular weight 30kDa), dissolve in 38g DMAc, Then, 2.0 g of non-solvent methanol was added thereto, and then mechanically stirred for 8 hours under the condition of 70° C. water bath to obtain a homogeneous solution, and left to defoam under the condition of 70° C. water bath. Then scrape the casting solution on a clean glass plate, after it is lowered to room temperature, then immerse it in the coagulation bath-water to solidify to form a film. The results show that the section of the blend membrane obtained under this condition is an asymmetric gradient open-pore sponge structure, and its pure water flux is 958L / m 2 h, the rejection rate of BSA is 97.8%, and the mechanical strength reaches 4.6MPa.

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Abstract

The invention discloses a method for preparing polymeric blend membrane by a nonsolvent induced gel phase separation method in the technical field of polymer membrane separation. The method comprisesthe following steps: firstly, preparing a polysulfone polymer, a water-insoluble hydrophilic sulfonated polymer, a pore-foaming agent, a non-soluble additive and a solvent into a homogeneous membranecasting solution at a certain temperature; then pouring the homogeneous membrane casting solution onto a glass plate, coating into a membrane by using a scraper, and cooling to room temperature to gelthe membrane; finally, immersing in a coagulation bath and curing into the membrane. By the method, through introduction of the sulfonated polymer for blend modification, the permanent hydrophilicityand pollution resistance of the membrane are achieved; a gelation system formed by the interaction of hydrogen bonds between a nonsolvent and the hydrophilic polymer is stable, so that occurrence ofmacropores can be effectively inhibited, the prepared blend membrane is a gradient asymmetric sponge structure and has high pure water flux and excellent mechanical properties and separation performance; in addition, the method is easy to implement industrially.

Description

technical field [0001] The invention belongs to the technical field of polymer membrane separation, in particular to a method for preparing a polymer blend membrane by a non-solvent-induced gel phase separation method. Background technique [0002] Membrane separation technology is a new type of separation technology that emerged in the mid-1960s. Due to its small footprint, high separation efficiency, low energy consumption, simple and safe operation, it is widely used in water treatment, food, medicine, chemical and other fields. Separation membrane structure and performance are important factors to determine its application. The polymer membrane network pore structure (such as sponge structure) can effectively improve the phenomenon of compaction and collapse during operation. At the same time, the excellent anti-fouling performance of the polymer membrane can effectively inhibit membrane fouling, thereby effectively improving its separation efficiency and operational s...

Claims

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Application Information

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IPC IPC(8): B01D71/68B01D67/00
CPCB01D67/0011B01D67/0016B01D71/68
Inventor 李建新张雷崔振宇胡梦洋李建何本桥
Owner TIANJIN POLYTECHNIC UNIV