Preparation method of polyolefin microporous membrane

A technology of polyolefin microporous membrane and polyolefin resin, which is applied in the field of preparation of polyolefin microporous membrane, can solve the problems of uneven microporous membrane structure, low product yield, large equipment investment, etc. The effect of slipping, small investment, and small footprint

Active Publication Date: 2010-06-09
SHENZHEN SENIOR TECH MATERIAL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the step-by-step stretching process, due to the existence of a large amount of diluent in the formulation, after thermally induced phase separation, there is a large amount of diluent liquid on the surface of the cast sheet, and after entering the longitudinal stretching rollers, during the stretching process between the rollers due to Slipping leads to uneven structure and large thickness deviation of the final microporous membrane; and then in the process of horizontal stretching, due to the inherent tensile characteristics of horizontal stretching, the film is thicker on both sides and thinner in the middle, which also leads to uneven structure
In the process of synchronous stretching, although the slipping problem of longitudinal stretching is solved, on the one hand, it is the same as step stretching, and waste edges need to be cut off, resulting in low product yield; on the other hand, the investment in equipment is relatively large

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] 10% (weight) of high-density polyethylene (melting point 133° C.) is dropped into a twin-screw extruder (78 mm in diameter, L / D=50, strong mixing type), and 90 % (weight) of liquid paraffin (kinematic viscosity 90cst / 40°C), melted and kneaded under the conditions of 200°C and 150 rpm to form a solution, and passed the solution through an annular die (die lip opening 0.8mm, die Head temperature 200°C), blow molding film bubbles and cooling by cooling ring, blow up ratio 1, traction ratio 1, after lamination, shape treatment, processing temperature 100°C, processing time 10s; finally use methyl ethyl ketone to extract the liquid in the film Paraffin wax, after drying, carry out setting treatment at 100°C, with a stretching ratio of 1.0 times, and then wind up the finished polyolefin microporous membrane.

Embodiment 2

[0028] 60% (weight) of polypropylene (melting point 167° C.) is dropped into a twin-screw extruder (78 mm in diameter, L / D=50, strong mixing type), and 40% ( Weight) of solid paraffin, melted and kneaded under the conditions of 200 ° C and 150 rpm to form a solution, passed the solution through an annular die (the opening of the die lip is 0.8 mm, and the temperature of the die head is 180 ° C), blown into a film Bubble and cool through the cooling ring, the blowing ratio is 5, the traction ratio is 5, and after lamination, the processing temperature is 150°C, and the processing time is 100s; finally, the liquid paraffin in the film is extracted with methyl ethyl ketone, and after drying, the setting processing is carried out at 150°C , the stretching ratio is 1.5 times, and the finished polyolefin microporous membrane is rolled up after the finished product is obtained.

Embodiment 3

[0030]Put 20% (weight) of high-density polyethylene (melting point 133°C) into a twin-screw extruder (78mm in diameter, L / D=50, strong mixing type), and add 80% of it through the side feeding port with a metering pump. The dioctyl phthalate of % (weight), under the condition of 200 ℃, 150 rev / mins, melting kneading is modulated into solution, and this solution is passed through annular die head (die lip opening degree 0.8mm, die head temperature 240 ℃), blow molded film bubbles and cooled by cooling ring, blow up ratio 3, traction ratio 3, after lamination, setting treatment, treatment temperature 125 ℃, treatment time 10s; finally use butanone to extract phthalic acid in the film Dioctyl ester, after drying, carry out setting treatment at 125°C, and the stretching ratio is 1.4 times, and the finished polyolefin microporous membrane is obtained and rolled up.

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Abstract

The invention provides a preparation method of polyolefin microporous membrane, comprising the following steps of: (1) mixing polyolefin resin and diluent according to the weight percent ratio of 10-60%:40-90%; (2) extruding and molding the mixture in an extrusion-blow molding manner to form bubble and cooling; (3) sizing the superposed and drawn membrane; (4) extracting diluent and drying; (5) performing transverse stretching and sizing treatment; and (6) rolling. By adopting the method of forming the bubble in a blow molding way, the invention avoids uneven structure caused by different cooling on the both surfaces in the casting process of general bidirectional stretching technique as well as uneven structure caused by slippage during longitudinal stretching, solves the problem of slippage of rollers during longitudinal stretching and ensures balanced longitudinal and transverse properties to finally obtain the polyolefin microporous membrane with even structure. Besides, the invention has the advantages of little investment, small occupation area, no slitter edge, easily-controlled production field, and the like.

Description

technical field [0001] The invention relates to a preparation method of a plastic film, in particular to a preparation of a polyolefin microporous film. Background technique [0002] Polyolefin microporous film is a plastic film with numerous interconnected micropores with a pore size of 0.01-10 μm. Its preparation methods mainly include: stretching high-filling plastic film method, melt stretching method, heat-induced phase separation method, hollow fiber method, physical and mechanical perforation method, etc. Among them, the industrialized methods mainly include melt stretching method and thermally induced phase separation method. [0003] The melt stretching method is to extrude a crystalline polymer (such as polypropylene) into a film under the condition of increasing the stress of the molten polymer, and then anneal the film under no tension or low tension to obtain the necessary crystal structure, and then carry out longitudinal stretching. Stretching creates a netw...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08J9/00C08J9/28C08J9/26C08L23/00C08L23/06C08L23/12C08L23/16C08L23/08C08L23/20C08K13/02B29C49/04B29C47/92B29C55/04B29C49/78B29C48/92
CPCC08J2323/02B29C55/08B29K2023/00B29C55/18B29L2031/755B29C55/28B29C47/0026B29K2105/04C08J5/18C08L23/02B29C48/10B29C48/92B29C2948/92561B29C2948/92704B29C2948/92895B29C2948/92923B29C2948/92942
Inventor 陈秀蜂高东波陈勇杨梅
Owner SHENZHEN SENIOR TECH MATERIAL
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