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Amphipathic starlike three-arm polyvinylidene fluoride block copolymer

A polyvinylidene fluoride and block copolymer technology, which is applied in the field of amphiphilic star-shaped three-arm polyvinylidene fluoride block copolymer and its preparation, can solve the problems of uncontrollable graft length, low graft rate, and poor grafting. The problem of uneven distribution of branch segments, etc., achieves a good three-dimensional hydrophilic structure, avoids unstable groups, and improves the effect of hydrophilicity

Active Publication Date: 2018-12-11
UNIV OF JINAN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, graft copolymerization has disadvantages such as low grafting rate, uneven distribution of grafted segments, and uncontrollable graft length, which affect the hydrophilic modification effect of PVDF membranes.

Method used

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  • Amphipathic starlike three-arm polyvinylidene fluoride block copolymer
  • Amphipathic starlike three-arm polyvinylidene fluoride block copolymer
  • Amphipathic starlike three-arm polyvinylidene fluoride block copolymer

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] A preparation method of an amphiphilic star-shaped three-arm polyvinylidene fluoride block copolymer, comprising the steps of:

[0040] In a 1L reactor, add 500 g of N,N-dimethylformamide, (CF 3 CF 2 (CF 2 OCF (CF 3 )) 2 COO) 2 Initiator 2.03g, HOCH 2 C(CH 2 CH 2 SC(=S)OCH 2 CF 3 ) 3 2.08 g of chain transfer agent, lower the temperature to 0°C, slowly pass through nitrogen for 30 minutes, remove the oxygen in the system, and fill with 96.0 g of vinylidene fluoride and 165.0 g of CO 2; The temperature was raised to 35°C to start polymerization, the polymerization pressure was 16 MPa, the reaction time was 12 h and cooled to room temperature to complete the polymerization, and the unreacted VDF monomer was recovered to obtain polyvinylidene fluoride active macromolecules. Continue to add 15.8 g of vinyl acetate and 0.65 g of azobisisobutyronitrile into the kettle, start stirring and raise the temperature to 70°C to continue the reaction for 12 h, then stop, add...

Embodiment 2

[0046] In a 1L reactor, add 500 g of N,N-dimethylformamide, (CF 3 CF 2 (CF 2 OCF (CF 3 )) 2 COO) 2 Initiator 2.03g, HOCH 2 C(CH 2 CH 2 SC(=S)OCH 2 CF 3 ) 3 2.08 g of chain transfer agent, lower the temperature to 0°C, slowly pass through nitrogen for 30 minutes, remove the oxygen in the system, and fill in 128.0 g of vinylidene fluoride and 163.5 g of CO 2 ; The temperature was raised to 35°C, the polymerization pressure was 17MPa, the polymerization was started, the reaction time was 12 h, the polymerization was completed after cooling to room temperature, and the unreacted VDF monomer was recovered to obtain polyvinylidene fluoride active macromolecules. Add 15.8 g of vinyl acetate and 0.65 g of azobisisobutyronitrile into the kettle, start stirring and raise the temperature to 70°C to continue the reaction for 12 h, then stop, add methanol / water (volume ratio 1:1) to obtain a white precipitate, filter in a vacuum Dry to obtain PVDF-PVAc block copolymer.

[0047]...

Embodiment 3

[0052] In a 1L reactor, add N,N-dimethylformamide 500g, (CF 3 CF 2 (CF 2 OCF (CF 3 )) 2 COO) 2 Initiator 1.95 g, HOCH 2 C(CH 2 CH 2 SC(=S)OCH 2 CF 3 ) 3 Chain transfer agent 1.63 g, cool down to 0 °C, slowly pass through nitrogen for 30 minutes, remove the oxygen in the system, fill with 128.0 g of vinylidene fluoride and 174.0 g of CO 2 ; The temperature was raised to 35°C, the polymerization pressure was 28MPa, the polymerization was started, the reaction time was 12 h, the polymerization was completed after cooling to room temperature, and the unreacted VDF monomer was recovered to obtain polyvinylidene fluoride active macromolecules. Add 18.5 g of vinyl acetate and 0.65 g of azobisisobutyronitrile into the kettle, start stirring and raise the temperature to 70°C to continue the reaction for 12 hours, then stop, add methanol / water (volume ratio 1:1) to obtain a white precipitate, filter and dry in vacuo A PVDF-b-PVAc block copolymer is obtained.

[0053] Take 2...

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Abstract

The invention relates to an amphipathic starlike three-arm polyvinylidene fluoride block copolymer and a preparation method thereof and belongs to the technical field of fluorine-containing polymers.The block copolymer is composed of a polyvinylidene fluoride chain segment (PVDF), a polyvinyl acetate (PVAc) chain segment and a polyvinyl alcohol (PVA) chain segment. The structural formula of the block copolymer is as shown in a formula. The amphipathic starlike three-arm polyvinylidene fluoride block copolymer is composed of the polyvinylidene fluoride chain segment, the polyvinyl acetate chain segment and the polyvinyl alcohol chain segment. The lengths of different chain segments, proportion of two blocks and molecular weight of the polymer can be controlled and adjusted by means of adding amount, reaction time, polymerizing pressure and the like of a monomer an a chain transfer agent. The amphipathic starlike three-arm polyvinylidene fluoride block copolymer also has good mechanicalproperties while has relatively good hydrophilicity.

Description

technical field [0001] The invention relates to an amphiphilic star-shaped three-arm polyvinylidene fluoride block copolymer and a preparation method thereof, belonging to the technical field of fluorine-containing polymers. Background technique [0002] Fluoropolymer materials are high-performance organic materials with excellent comprehensive properties, and are good substrates for preparing separation membranes. Polyvinylidene fluoride (PVDF) resin is the first choice for water treatment separation membrane because of its outstanding chemical stability, thermal stability and mechanical strength. However, PVDF has strong hydrophobicity, which leads to low water flux after film formation, and is prone to adsorption pollution, which seriously affects the separation performance and service life of the membrane, and increases the operating cost. Therefore, the hydrophilic modification of PVDF membrane is particularly important. [0003] At present, there are two types of hyd...

Claims

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Application Information

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IPC IPC(8): C08F293/00C08F8/06C08F8/12
CPCC08F8/06C08F8/12C08F293/005C08F2438/03
Inventor 徐安厚陈慧颖霍志远李文薇张书香
Owner UNIV OF JINAN