Method for producing polyolefin porous film, and laminated porous film
US-2015004466-A1 · Jan 1, 2015 · US
US10090500B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10090500-B2 |
| Application number | US-201715682857-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 22, 2017 |
| Priority date | Sep 20, 2016 |
| Publication date | Oct 2, 2018 |
| Grant date | Oct 2, 2018 |
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A film-stretching apparatus in accordance with an embodiment of the present invention includes a stretching furnace having (i) an entrance through which a material film is transferred into the stretching furnace and (ii) an exit through which the material film having been stretched is transferred out of the stretching furnace. An airflow in the entrance is controlled so as to be directed toward an inside of the stretching furnace. A gas in the stretching furnace is controlled so as to be discharged outside the stretching furnace.
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The invention claimed is: 1. A method of producing a film, the method comprising: a film stretching step of stretching a film, the film stretching step being carried out by use of a film-stretching apparatus which includes a stretching furnace having (i) an entrance through which the film is transferred into the stretching furnace and (ii) an exit through which the film is transferred out of the stretching furnace, in the film stretching step, an airflow in the entrance being controlled so as to be directed toward an inside of the stretching furnace, and at least a part of a gas in the stretching furnace being controlled so as to be discharged outside the stretching furnace from a part of the stretching furnace which extends from the entrance to a location before the film starts to be stretched in a direction in which the film is transferred or in a width direction, the gas including air which has entered the stretching furnace from the entrance. 2. The method as set forth in claim 1 , further comprising controlling a pressure in the stretching furnace to be a negative pressure. 3. The method as set forth in claim 2 , wherein a difference between the pressure in the stretching furnace and atmospheric pressure is not smaller than 2 Pa. 4. The method as set forth in claim 3 , wherein the airflow directed toward the inside of the stretching furnace has an airflow rate of not less than 0.5 m/sec. 5. The method as set forth in claim 1 , further comprising, in the film stretching step, controlling an airflow in the exit so as to be directed toward the inside of the stretching furnace. 6. The method as set forth in claim 5 , further comprising controlling a pressure in the stretching furnace to be a negative pressure. 7. The method as set forth in claim 6 , wherein a difference between the pressure in the stretching furnace and atmospheric pressure is not smaller than 2 Pa. 8. The method as set forth in claim 7 , wherein the airflow directed toward the inside of the stretching furnace has an airflow rate of not less than 0.5 m/sec. 9. The method as set forth in claim 1 , wherein the stretching furnace is divided, along a direction in which the film is transferred, into a plurality of air amount control zones, and wherein the method further comprises independently controlling an amount of air in each of the air amount control zones. 10. The method as set forth in claim 9 , further comprising controlling a pressure in one of the plurality of air amount control zones which is connected to the entrance to be a negative pressure. 11. The method as set forth in claim 9 , further comprising independently controlling an operating temperature of each of the air amount control zones. 12. The method as set forth in claim 9 , wherein the plurality of air amount control zones includes a pre-heating chamber and at least a first stretching chamber. 13. The method as set forth in claim 12 , wherein a temperature in the pre-heating chamber is controlled within a range of 115° C. to 125° C. and wherein a temperature in the at least first stretching chamber is controlled within a range of 100° C. to 115° C. 14. The method as set forth in claim 12 , wherein the plurality of air amount control zones includes a heat-fixing chamber in which the film which has been stretched is heated while a width of the film which has been stretched is maintained. 15. The method as set forth in claim 14 , wherein a temperature in the heat-fixing chamber is controlled within a range of 115° C. to 130° C. 16. The method as set forth in claim 1 , further comprising pre-heating the film in the stretching furnace prior to stretching the film. 17. The method as set forth in claim 16 , wherein the film comprises a polyethylene-based resin. 18. The method as set forth in claim 17 , wherein the film stretching step is carried out at a temperature which is lower than a temperature to which the film has been pre-heated. 19. The method as set forth in claim 1 , wherein the film is uniaxially or biaxially stretched in the stretching furnace. 20. A method of producing a film, the method comprising: a film stretching step of stretching a film, the film stretching step being carried out by use of a film-stretching apparatus which includes a stretching furnace having (i) an entrance through which the film is transferred into the stretching furnace and (ii) an exit through which the film is transferred out of the stretching furnace, in the film stretching step, an amount of air to be discharged outside the stretching furnace from a part of the stretching furnace being controlled so as to be larger than an amount of air to be supplied to the part of the stretching furnace from the outside of the stretching furnace, the part of the stretching furnace extending from the entrance to a location before the film starts to be stretched in a direction in which the film is transferred or in a width direction.
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