Method for producing hollow fiber film

A hollow, melt-spinning technology, applied in membrane technology, semi-permeable membrane separation, chemical instruments and methods, etc., can solve problems such as inability to meet high-strength requirements, uneven dispersion, and uneven pore size distribution of porous membranes

Inactive Publication Date: 2010-04-28
TIANJIN POLYTECHNIC UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this method, uneven dispersion is likely to cause uneven pore size distribution of the formed porous membrane, and the water permeability of the membrane is small, which cannot meet the needs;
[0005] 2. In Japanese Patent Application Laid-Open No. 2002-253939, it is recorded that only film-forming polymers are used without additives, and the polymer is preformed into fibers and then stretched to cause pores. It is not easy to obtain high porosity, high water permeability, and pore size. Uniformly distributed hollow fiber membranes;
[0008] The hollow fiber membranes spun by the above existing technologies have weak film-forming strength and cannot meet the requirements of high strength.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Example 1: 1500 grams of calcium carbonate (2-5 microns in particle diameter) particles, 2000 grams of polyvinylidene fluoride resin, 500 grams of polyethylene glycol 20000, 100 grams of TW-20, 100 grams of glass fiber, and 1500 grams of ortho Dibutyl phthalate was blended and granulated at 220°C, and melt-spun. Use hydrochloric acid solution to remove calcium carbonate in polyvinylidene fluoride hollow fiber, remove dibutyl phthalate with isopropanol, and obtain polyvinylidene fluoride hollow fiber porous membrane with an inner diameter of 0.4 mm, an outer diameter of 0.6 mm, and a burst strength of 1.32 MPa, pure water penetration rate 970L / m 2·h@0.1MPa 20℃, membrane separation pore size 0.10μm, porosity 72%.

Embodiment 2

[0030] Example 2: 500 grams of aluminum oxide 20-80 nanoparticles, 2000 grams of polyvinylidene fluoride resin, 100 grams of TW-80, 100 grams of glass fiber, and 1500 grams of diethylene glycol dimethyl ether were heated at 215 ° C. Twin-screw blending, melt spinning. Use NaOH aqueous solution to remove Al2O3 in polyvinylidene fluoride hollow fiber, isopropanol to remove diethylene glycol dimethyl ether, and the obtained external pressure polyvinylidene fluoride hollow fiber porous membrane has an inner diameter of 0.5 mm and a wall thickness of 0.15 mm. Bursting strength 1.32MPa, pure water penetration rate 1270L / m 2 ·h@0.1MPa 20℃, membrane separation pore size 0.20μm, porosity 76%.

Embodiment 3

[0032] Example 3: 800 grams of calcium carbonate nanoparticles, 1800 grams of polyvinylidene fluoride resin, 780 grams of polyvinylpyrrolidone, 20 grams of fluorosurfactant FC-4, 800 grams of triethyl phosphate, and 100 grams of carbon fiber were mixed at 220 ° C Blending granulation, melt spinning. Use hydrochloric acid solution to remove calcium carbonate, triethyl phosphate, etc. in polyvinylidene fluoride hollow fiber, and the obtained polyvinylidene fluoride hollow fiber porous membrane has an inner diameter of 0.6 mm, an outer diameter of 1.0 mm, a burst strength of 1.23 MPa, and a pure water permeation rate of 1290L / m 2 ·h@0.1MPa 20℃, membrane separation pore size 0.50μm.

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PUM

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Abstract

The melt spinning process of producing hollow fiber membrane includes the first mixing glass fiber with inorganic particle, polymer pore creating agent, surfactant and non-solvent to constitute spinning composition, heating the composition to temperature higher than the smelting point of the polymer, the subsequent extruding the melt through spinning head and cooling to form hollow fiber, and final eliminating the inorganic particle, polymer pore creating agent, surfactant and non-solvent to produce the high strength hollow fiber membrane. The spinning composition consists of polymer 20-90 wt%, glass fiber 0.5-20 wt%, inorganic pore creating agent 5-50 wt%, polymer pore creating agent 2-30 wt%, surfactant 2-60 wt%, and organic non-solvent 10-60 wt%.

Description

technical field [0001] The invention relates to a method for producing a hollow fiber membrane by melt spinning. In the method, a non-melting fiber such as glass fiber is added to a film-forming polymer melt to obtain a hollow fiber membrane with high strength and uniform hole formation. Background technique [0002] Hollow fiber membranes are mainly used for filtration or dialysis in various fields. The hollow fiber membrane melt-spinning method of the present invention is to form a spinning composition with non-melting fibers such as glass fibers and inorganic particles, polymer porogens, surfactants and non-solvents, mix them uniformly and heat them above the melting temperature of the polymer, Then the melt is extruded in the spinning head, cooled to form a hollow fiber, and the hollow fiber membrane is made by removing inorganic particles, polymer porogens, surfactants and non-solvents. [0003] When spinning pure polymer hollow fibers, it is easy to form a water-imper...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D69/08
Inventor 吕晓龙
Owner TIANJIN POLYTECHNIC UNIV
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