JP2841817B2 - Method for producing thermoplastic resin film - Google Patents

Description

The present invention relates to a method for producing a thermoplastic resin film which is uniform in a lateral direction. More specifically, it suppresses the bowing phenomenon that occurs when the film is laterally stretched and thermally fixed by a tenter,
The present invention relates to a method for producing a thermoplastic resin film having uniform physical, chemical and physicochemical properties in a lateral direction.

(Prior art) Thermoplastic resin films, particularly films of biaxially oriented polyester, polyamide, polyolefin, polyvinyl resin, polyphenylene sulfide, etc.
It is used for packaging, industrial use, and other uses, and it is desirable that the film has the same physical properties at any portion in the lateral direction.

However, it has been extremely difficult to make the physical properties of the product film uniform in the lateral direction by the conventional manufacturing method. The reason is that both ends of the film are gripped by the clips in the tenter, and the longitudinal stretching stress generated by the stretching process and the shrinkage stress generated by the heat fixing process are restrained by the clips serving as the gripping means. On the other hand, it is known that the influence of the gripping means is low at the central portion of the film and the binding force is weak, and that the central portion of the film is delayed with respect to the end portion gripped by the clip due to the above-mentioned stress. And when performing horizontal stretching and heat setting continuously with the same tenter, if a straight line is drawn along the horizontal direction on the surface of the film before entering the tenter, this straight line will be deformed in the tenter and the film will be deformed. With respect to the traveling direction of the stretching process, the film deforms into a convex shape at the beginning of the stretching process, returns straight in the region immediately before the end of the stretching process, and deforms into a concave shape after the stretching process. Furthermore, at the beginning of the heat setting step, the concave deformation reaches a maximum value, the curve remains unchanged and passes through the subsequent tenter, leaving the concave deformation in the film leaving the tenter. This phenomenon is called a bowing phenomenon, and this bowing phenomenon causes unevenness in the physical properties of the film in the lateral direction. Due to the bowing phenomenon, an inclined main axis is generated at a side end portion of the film, and the angle of the main axis in the lateral direction tends to be different. As a result, for example, the thermal contraction rate in the longitudinal direction, the thermal expansion rate,
Physical properties such as wet swelling coefficient differ in the lateral direction of the film.

Due to the bowing phenomenon, as an example of packaging applications, it causes troubles such as printing pitch deviation, unevenness, curling, meandering, and the like in a printing lamination process, a bag making process, and the like. Further, as an example of industrial use, in a base film such as a floppy disk, in-plane anisotropy causes trouble such as deterioration of magnetic recording characteristics.

More specifically, as a conventional technique for providing a cooling step between the horizontal stretching and the heat setting, Japanese Patent Publication No. 35-11774 discloses a method in which a relaxation step of 20 ° C. to 150 ° C. is interposed between the horizontal stretching and the heat fixing step. A manufacturing method having a substantial cooling step has been proposed. However, the length of the cooling step is not described at all, and the effect of reducing the bowing phenomenon is not completely known. Further, as a technique for reducing or eliminating the bowing phenomenon, Japanese Patent Application Laid-Open No. 50-73978 proposes a method for producing a film in which a nip roll group is provided between a stretching step and a heat setting step. However, in this technique, the temperature of the intermediate zone where the nip roll is installed is equal to or higher than the glass transition temperature, and the rigidity of the film at the nip point is low.

Japanese Patent Publication No. Sho 63-24459 proposes a process of forcibly advancing only a narrow area near the center by a nip roll while gripping both ends of the film after completion of the transverse stretching. However, in this technology, it is necessary to install the nip roll in a high-temperature area in the tenter, it is necessary to cool the roll and its peripheral devices, and since the film is high in temperature, there is a possibility that the roll may be damaged, so that it is not practical. Constrained by JP-B-62-43856 proposes a technique in which a film immediately after transverse stretching is cooled to a glass transition temperature or lower, and then heat-fixed in multiple stages to simultaneously stretch in the transverse direction at the same time as heat fixing. However, with this technology, because the cooling process has little decrease in the bowing phenomenon,
Or, because the bowing phenomenon is likely to occur again due to the heat setting, the process involves a multi-step heat setting and re-stretching in addition to the cooling step. Therefore, there is a concern that it may be difficult to stably control the ambient temperature and the film temperature in the tenter for a long time. Also, this proposal does not describe the relationship between the length of the cooling step and the film width. Further, JP-A-62-183327 discloses that, after longitudinal stretching, transverse stretching with a tenter and heat fixing, only the side end portion between the transverse stretching zone and the heat fixing zone has a glass transition temperature or higher heat fixing temperature. A technique for setting a preheating zone at the following temperatures has been proposed. However, in this technique, since it is necessary to control the temperature of the preheating zone while giving a temperature gradient in the lateral direction, there is a concern that it may be difficult to control the film temperature for a long time. In the embodiment of the present invention, since the length of the preheating zone is as short as half of the film width, it is assumed that the effect of reducing the bowing phenomenon is small. Also,
Japanese Patent Application Laid-Open No. 1-165423 proposes a technique in which a film after transverse stretching is cooled to a temperature equal to or lower than the transverse stretching temperature and then stretched again in the transverse direction while increasing the temperature in multiple stages. However, in this technique, as in the case of Japanese Patent Publication No. 62-43856, the effect of reducing the bowing phenomenon in the cooling step is small, or because the bowing is likely to occur in the heat fixing step, In addition, it is a complicated step of a step of heat setting in multiple stages and a step of re-stretching.

Therefore, there is a concern that it may be difficult to stably control the ambient temperature and the film temperature in the tenter for a long time. In the present proposal, it is described that the length of the cooling step is preferably equal to or more than の of the film width, but the basis is not clear. Further, it is described that the cooling temperature is preferably equal to or higher than the glass transition temperature and equal to or lower than the stretching temperature. However, if the length of the cooling step or the temperature of the cooling step is equal to or higher than the glass transition temperature, it is feared that the effect of reducing the bowing phenomenon is small, and it is presumed that the above complicated steps have to be adopted. Is done. In addition, Japanese Patent Publication Nos. 1-25694 and 1-25696 propose a technique in which the running direction of a film is reversed to perform transverse stretching and heat fixing. However, in this technique, it is necessary to wind the film once in order to reverse the running direction of the film, and there is a problem in that it is an off-line manufacturing method, so that productivity is restricted.

(Problems to be Solved by the Invention) In order to solve such problems, it is an object of the present invention to provide a method for producing a film having uniform properties in the lateral direction, which is industrially advantageous (particularly, physical property values such as heat shrinkage).

(Means for Solving the Problems) The present inventors have observed the change of the bowing line in the tenter, clarified the generation process of the bowing phenomenon from various studies, and examined means for reducing the bowing phenomenon. The present invention has been reached.

In the present invention, in producing a thermoplastic resin film stretched at least in the transverse direction, the transversely stretched film is relaxed in the transverse direction by a cooling step satisfying the formula (1) below the transverse stretching temperature, This is a method for producing a thermoplastic resin film, characterized by being fixed.

L / W ≧ 1.0 (1) In the equation (1), L is the length (m) of the cooling step.
And W means the distance (m) between the clips of the tenter at the tenter outlet. The length L of the cooling step means the length from the point where the transverse stretching is 80% or more of the desired transverse stretching ratio to the longest point from the temperature of the cooling step to the temperature of the next step which is substantially higher. I do. Further, the lateral direction means a direction perpendicular to the running direction of the film, and the vertical direction means the running direction.

Also, the value of the ratio L / W of the length L of the cooling step to the film width W does not essentially depend on the speed of the tenter, but as the speed of the tenter increases, the temperature of the film becomes substantially more effective. It takes time to reach the temperature, and the ratio L / W of the length L of the cooling step to the width W of the film, which is the gist of the present invention.
Becomes substantially smaller.

Therefore, when the tenter speed is increased, the effect is improved as the ratio L / W of the length L of the cooling step to the film width W is increased. For example, when the tenter speed is doubled, the ratio L / W of the length L of the cooling step to the film width W is obtained.
Is preferably selected to be at least 1.5 times the value before the speed increase.

 Hereinafter, the present invention will be described in detail.

In the present invention, the thermoplastic resin is heated and melted to a temperature equal to or higher than its melting point, extruded in the form of a film from the extrusion means including a slit die to the surface of the cooling drum, and stretched in the longitudinal direction by a group of rolls having different longitudinal roll speeds. It is known that the film is stretched in a transverse direction by a tenter, and if necessary, is heat-set and wound up by a film winder or the like. In the present invention,
As the film forming / stretching conditions, such resin melting / extrusion conditions, casting conditions, longitudinal stretching conditions, transverse stretching conditions, heat setting conditions, winding conditions, and the like can be appropriately selected. Further, in the present invention, a stretching method other than the production method of performing the transverse stretching after the longitudinal stretching is also included in the present invention. For example, a stretching method in which longitudinal stretching is performed again after longitudinal and transverse stretching, a stretching method including longitudinal multi-stage stretching, and a stretching method in which both ends of a film after transverse stretching are vertically stretched by trimming both ends are not limited to those described above unless the gist is exceeded. Absent.

As the thermoplastic resin applied to the present invention, polyethylene terephthalate, polyethylene 2,6-naphthalate, polyethylene isophthalate, polyester resin such as polybutylene terephthalate, nylon-6, polyamide resin such as nylon-66, polypropylene,
Polyolefin resins such as polyethylene, polyphenylene sulfide, polyether sulfone, polysulfone, polyether ether ketone, polyether ketone ketone, polyethylene trimellited imide, and many other simple substances, copolymers, mixtures, composites, and the like. Can be

The production method of the present invention transversely stretches the thermoplastic resin film,
At the time of the heat setting treatment, the film after the completion of the transverse stretching step is cooled to a stretching temperature or lower and simultaneously relaxed in the transverse direction to reduce the bowing phenomenon generated in the transverse stretching step. The greater the value of the ratio L / W between the length L of the cooling step and the film width W, the greater the effect of reducing the bowing phenomenon, and the ratio of the flow rate L to the film width W of the cooling step is L / W ≧ 2.0. It is preferable to select the length L of the cooling step. More preferably, L / W ≧ 3.0.

Further, when the tenter for performing the transverse stretching step and the heat setting step is cut off, the film is cooled in order to run the film in the atmosphere, so that the ratio L / W of the length L of the cooling step to the film width W is used. As long as the condition of ≧ 1.0 is satisfied, it is included in the present invention that the transverse stretching step and the heat setting step are performed by different tenters.

Further, in the cooling step and the cooling step after the heat fixing step, it is preferable to pass the film through a group of nip rolls whose speed can be controlled, and the effect is remarkably improved. The material of the nip roll is a combination of a metal mirror surface and a rubber elastic body, and the nip roll tensions the film at a speed relative to the clip of the tenter, so that the speed control is easy. Preferably, both nip rolls are mutually controllable.

Conventionally, in order to reduce the heat shrinkage rate in the horizontal direction, a method has been adopted in which the space between the clips of the tenter is narrowed after the heat fixing step or at the same time as the heat fixing step so as to relax in the horizontal direction. However, in this method, the bowing phenomenon tends to increase as the relaxation in the lateral direction increases. Therefore, the present invention has found a technique for reducing the bowing phenomenon and at the same time improving the physical properties of the film by relaxing the film in the transverse direction in the cooling step after the completion of the transverse stretching. According to this technique, the propagation of stretching stress generated during transverse stretching can be controlled, and the property value such as the heat shrinkage of the film can be improved by relaxing the stretching in the transverse direction in the cooling step. Here, the relaxation rate in the horizontal direction in this cooling step is preferably 10% or less from the viewpoint of film wrinkling or the like, and more preferably 5% or less. In addition, this relaxation rate means the value based on the film width at the time of completion of transverse stretching.

In the present invention, the reason why an industrially advantageous effect can be obtained when producing a film having a small bowing phenomenon is that no one can do it in determining the length of the cooling step necessary to reduce the bowing phenomenon. A numerical model that can apply the finite element method is set and the propagation of stretching stress can be estimated by numerical analysis. As a result, the stress at the ratio L / W of the length L of the cooling process to the width W of the film L / W = 1.0 is obtained. Propagation is about 1/2, and L / W = 2.0, stress propagation is about 1/10, 1
This is because it was found from the calculated value that / W = 3.0 became almost zero, which was confirmed by the actual machine, and found to be applicable in any case.

 Next, examples will be described.

(Example) An example of an apparatus used in the present invention will be described. The thermoplastic resin extruded from the T-die is rapidly cooled by a chill roll and formed into a film. The film is stretched in the machine direction by a roll stretching machine, and then passed through a preheating zone and into a transverse stretching zone while being gripped at both ends by clips of a tenter, and is transversely stretched. In addition, the film enters the cooling zone and is relaxed laterally,
After passing through the heat setting zone and being heat set, it is released from the clip, exits the tenter and wound by the winder.

 Hereinafter, a description will be given with some examples.

Example 1 A polyethylene terephthalate resin was dissolved, extruded from a T-die, and formed into a film on a chill roll.
A biaxially oriented polyethylene terephthalate film was obtained by setting the stretching ratio in the longitudinal direction by a roll stretching machine to 3.5 times and then increasing the stretching ratio in the transverse direction by a tenter to 3.5 times. As for the temperature in the tenter, the preheating temperature is 90 ° C and the stretching temperature is
The cooling temperature was 80 ° C., the heat setting temperature was 220 ° C., and the ratio L / W of the length L of the cooling zone to the film width W was 2.0.
Furthermore, the relaxation rate in the horizontal direction in the cooling step was 3%, and the relaxation rate in the horizontal direction in the heat fixing step was 2%.

Example 2 In Example 1, the relaxation rate in the lateral direction in the cooling step was 8
%, And a biaxially oriented polyethylene terephthalate film was obtained in the same manner as in Example 1 except that the relaxation rate in the horizontal direction in the heat fixing step was set to 0%.

Comparative Example 1 In Example 1, the relaxation rate in the transverse direction in the cooling step was set to 0.
%, And a biaxially oriented polyethylene terephthalate film was obtained in the same manner as in Example 1 except that the relaxation rate in the horizontal direction in the heat fixing step was 5%.

Example 3 Nylon-6 resin was melted, extruded from a T-die, formed into a film on a chill roll, and then stretched in a longitudinal direction by a roll stretching machine to 3.3 times, and then stretched in a transverse direction by a tenter to 3.4 times. As a result, a biaxially oriented nylon-6 film was obtained. The temperature in the tenter was 60 ° C for the preheating temperature, 85 ° C for the stretching temperature, 60 ° C for the cooling temperature, 215 ° C for the heat setting temperature, the length L of the cooling zone and the width W of the film.
L / W = 2.0. Further, the relaxation rate in the horizontal direction in the cooling step is 4%, and the relaxation rate in the horizontal direction in the heat fixing step is 1%.
%.

Comparative Example 2 In Example 3, the relaxation rate in the lateral direction in the cooling step was set to 0.
%, And a biaxially oriented nylon-6 film was obtained in the same manner as in Example 3 except that the relaxation rate in the horizontal direction in the heat fixing step was 5%.

Table 1 shows the film forming conditions and the measurement results of the bowing distortion in the comparative example of the example. Boeing distortion is drawn on the surface of the film before entering the tenter by a straight line, and is shown in Fig. 1 on the finally obtained film. B = b / W × 100 (%) where B = Boeing distortion amount (%) W = Film width (mm) b = Boeing line The maximum swelling amount (mm) was calculated.

(Effects of the Invention) Comparative Example (when relaxation is not performed in the lateral direction in the cooling step)
Means that bowing distortion is large, but in the embodiment of the present invention, it is possible to produce a film having uniform physical properties in the transverse direction of the film by suppressing the bowing phenomenon that occurs in the step of transversely stretching and heat setting the thermoplastic resin film. I understand.

[Brief description of the drawings]

 FIG. 1 shows a method of calculating the bowing distortion.

──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. ⁶ , DB name) B29C 55/02-55/16 C08J 5/18

Claims (1)

(57) [Claims] In producing a thermoplastic resin film stretched at least in the transverse direction, the transversely stretched film is relaxed in the transverse direction by a cooling step satisfying the formula (1) below the transverse stretching temperature. A method for producing a thermoplastic resin film, comprising heat setting. L / W ≧ 1.0 (1) In the equation (1), L is the length (m) of the cooling step.
And W means the distance (m) between the clips of the tenter at the tenter outlet.