Heat-shrinkable polyester film and package
a polyester film and heat shrinkage technology, applied in the direction of synthetic resin layered products, other domestic articles, sustainable manufacturing/processing, etc., can solve the problems of high temperature incineration, low heat resistance, and large black smoke accompanied by abnormal odor, and achieve small shrinkage stress, high followability, and sufficient heat shrinkage properties
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synthetic example 1
[0089]100 mol % of dimethyl terephthalate (DMT) as a dicarboxylic acid component and 100 mol % of ethylene glycol (EG) as a polyhydric alcohol component were placed in a stainless steel autoclave equipped with a stirrer, a thermometer and a partially circulating cooler such that the amount of ethylene glycol was 2.2 times the amount of dimethyl terephthalate in terms of the molar ratio, 0.05 mol % (based on the acid component) of zinc acetate was added as an ester exchange catalyst, 0.225 mol % (based on the acid component) of antimony trioxide was added as a polycondensation catalyst, and an ester exchange reaction was carried out while distilling away generated methanol to outside the system. Thereafter, a polycondensation reaction was carried out at 280° C. under a reduced pressure of 26.7 Pa to obtain polyester 1 having an intrinsic viscosity of 0.75 dl / g. The composition is shown in Table 1.
synthetic examples 2 to 7
[0090]Polyesters 2 to 4 shown in Table 1 were prepared in the same manner as in Synthetic Example 1. In the production of polyester 2, SiO2 (Silysia 266, manufactured by FUJI SILYSIA CHEMICAL LTD.; average particle diameter: 1.5 μm) was added as a lubricant at a proportion of 7,200 ppm relative to the polyester. In the Table, NPG is neopentyl glycol, BD is 1,4-butanediol, and DEG is diethylene glycol, which is a side product. The intrinsic viscosities of polyesters 2, 3 and 4 were 2: 0.75 dl / g, 3: 1.20 dl / g and 4: 1.20 dl / g, respectively. Each polyester was appropriately formed into a chip.
example 1
[0091]Polyester 1, polyester 2 and polyester 3 as described above were mixed in the mass ratio of 45:5:50 and the mixed resin was introduced into an extruder. The mixed resin was molten at 280° C. and extruded from a T-die and then quenched by winding it around a rotating metal roll set at a surface temperature of 30° C. to obtain an undrawn film with a thickness of 42 μm. Tg of the undrawn film was 75° C. The obtained undrawn film was introduced to a lengthwise drawing machine in which a plurality of rolls were continuously disposed, heated till the film temperature reached 80° C. on a preheating roll, and then lengthwise drawn by a roll drawing method at the draw ratio in the longitudinal direction of 3.5 times so as to allow the thickness of the film after drawing to be 12 μm. After lengthwise drawing, the film was cooled by a cooling roll whose surface temperature was set to 25° C., and then wound as a roll. The resulting film was evaluated for various properties in the above-me...
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