Method for producing microporous thermoplastic resin membrane
View Patent ↗A method for producing a thermoplastic resin micro-porous film wherein a thermoplastic resin and a solvent (A) are melted and kneaded together to prepare a solution, the solution is extruded and cooled to prepare a formed product in a gel state, and the residual solvent (A) is removed from the formed product, characterized in that in the step of removing the solvent (A) use is made of a non-aqueous solvent (B) which is compatible with the solvent (A) and not compatible with the thermoplastic resin, and has a boiling point of 100° or higher and a flashing point of 0° or higher. The use of the non-aqueous solvent (B) provides a production method which allows the removal of a solvent with good efficiency and also with the reduction of a fear of environmental pollution and catching fire.
1. A method for producing a microporous thermoplastic resin membrane consisting essentially of the steps of extruding a solution obtained by melt-blending a thermoplastic resin and a solvent (A), cooling the resultant extrudate to form a gel-like product, stretching said gel-like product to form a stretched membrane having oriented molecular chains, and cleansing said stretched membrane to remove said solvent (A) remaining therein, wherein said solvent (A) is removed by two or more cleansing steps, at least one step among the cleansing steps using a nonaqueous solvent (B) in an amount of 300 to 30,000 parts by weight per 100 parts by weight of said gel-like molding, and a solvent (C) causing no depletion of an ozone layer and having a boiling point of 100° C. or lower being used at a final step, and wherein said solvent (C) is (a) hydrofluoroethers, or (b) a mixture of hydrofluoroethers and an alcohol having 3 or 4 carbon atoms, wherein said stretching is biaxial stretching and said biaxial stretching is simultaneous or sequential stretching in longitudinal and transverse directions, wherein said stretching is carried out at a temperature in a range between the crystalline dispersion temperature and under the crystalline melting point of said gel-like product, and wherein said stretching temperature is 110° C. to 120° C., wherein in the at least one step among the cleansing steps using the non-aqueous solvent (B) and in the final step using solvent (C), both non-aqueous solvent (B) and solvent (C) different from each other,
wherein in the at least one step using the non-aqueous solvent (B) and in the final step using solvent (C), both solvent (B) and solvent (C) are not used together in the at least one step and the final step.
2. The method for producing a microporous thermoplastic resin according to claim 1 , wherein said nonaqueous solvent (B) is at least one selected from the group consisting of paraffinic hydrocarbons, aromatic hydrocarbons, alcohols, esters, ethers and ketones.
3. The method for producing a microporous thermoplastic resin according to claim 1 , wherein said nonaqueous solvent (B) contains at least one solvent selected from the group consisting of linear hydrofluorocarbons, hydrofluoroethers and cyclic hydrofluorocarbons as a component (B′).
4. The method for producing a microporous thermoplastic resin according to claim 3 , wherein said linear hydrofluorocarbon is represented by the formula C 5 H 2 F 10 , said hydrofluoroether is represented by the formula C 4 F 9 OCH 3 or C 4 F 9 OC 2 H 5 , and said cyclic hydrofluorocarbon is represented by the formula C 5 H 3 F 7 .
5. The method for producing a microporous thermoplastic resin according to claim 1 , wherein said hydrofluoroether is represented by the formula C 4 F 9 OCH 3 or C 4 F 9 OC 2 H 5 .
6. The method for producing a microporous thermoplastic resin according to claim 1 , wherein said solvent (A) is removed before and/or after stretching said gel-like product.
7. The method for forming a microporous thermoplastic resin membrane according to claim 5 , wherein said microporous thermoplastic resin membrane has a thickness of 29-48 μm, a permeability of 190-1,070 sec/100 cc and a porosity of 35-70 volume % with a residue of 0.8-2.7 weight %.
8. The method for forming a microporous thermoplastic resin membrane according to claim 5 , wherein said thermoplastic resin is a polyolefin which has a weight-average molecular weight of 5×10 5 or more.
9. The method for forming a microporous thermoplastic resin membrane according to claim 5 , wherein said thermoplastic resin is a composition comprising ultra-high-molecular-weight polyethylene having a weight-average molecular weight of 5×10 5 or more and high density polyethylene having a weight-average molecular weight of 1×10 4 or more and less than 5×10 5 .
10. The method for producing a microporous thermoplastic resin according to claim 5 , wherein said composition has a ratio of weight-average molecular weight/number-average molecular weight (Mw/Mn) of 5 to 300.
11. The method for producing a microporous thermoplastic resin membrane according to claim 1 , wherein said alcohol having 3 or 4 carbon atoms in said mixture contained in said solvent (C) is at least one selected from the group consisting of n-propanol, isopropanol, s-butanol and t-butanol.
12. The method for producing a microporous thermoplastic resin membrane according to claim 1 , wherein said microporous thermoplastic resin membrane has a thickness of 29-48 μm, a permeability of 190-1,070 sec/100 cc and a porosity of 35-70 volume % with a residue of 0.8-2.7 weight %.
13. The method for producing a microporous thermoplastic resin according to claim 12 , wherein said thermoplastic resin is at least one polyolefin selected from the group consisting of polyethylene, polypropylene and polybutene-1.
14. The method for producing a microporous thermoplastic resin according to claim 1 , wherein said thermoplastic resin is selected from the group consisting of polyolefins, polyesters, polyamides and polyallylene sulfides.
15. The method for producing a microporous thermoplastic resin according to claim 1 , wherein the stretching magnification in said biaxial stretching is at least twice or more in any direction and 10 times or more by area magnification.
16. The method for producing a microporous thermoplastic resin according to claim 1 , wherein said stretching is carried out by a method of any one of a tenter method, a roll method, an inflation method, a rolling method or a combination thereof.
17. The method for producing a microporous thermoplastic resin according to claim 1 , wherein biaxial stretching is at least twice or more in any direction and 10 times or more by area magnification.
18. The method for producing a microporous thermoplastic resin according to claim 1 , wherein said cleansing step is carried out by a method of extracting by immersion in a nonaqueous solvent (B), a method of spraying a nonaqueous solvent (B), or a combination thereof.