Piled sheet and process for producing the same
a technology of piled sheets and piled sheets, which is applied in the field of raised sheets, can solve the problems of easy deformation, strained chair covering fabric, and hand fatigue, and achieve the effects of good copolymerization, good melt spinnability, and good copolymerization
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production example 1
Production of Polyurethane Sheet B
[0044]Into a screw kneading polymerizer, poly-3-methyl-1,5-pentyl adipate glycol having an average molecular weight of 1150, polyethylene glycol having an average molecular weight of 2000, 4,4′-diphenylmethane diisocyanate, and 1,4-butanediol were charged in a molar ratio of 0.9:0.1:4:3 (4.63% of theoretical amount of nitrogen when calculated based on the amount of isocyanate group), and then the melt polymerization was allowed to proceed to produce polyurethane. The heat softening point of polyurethane was 125° C. The molten polyurethane was melt-blown to form a random web as follows. The molten polyurethane was extruded from the slots on a die orifice heated at 260° C. The fibrous molten polyurethane was made into fine fibers Abets by an air jet of 260° C. and collected on a wire cloth moving at 2 m / min at a collection distance of 40 cm. The obtained melt-blown polyurethane nonwoven fabric B was composed of fine fibers of about 0.13 dtex and had a...
production example 2
Production of Woven Fabric C
[0045]Polyester yarns (80 dtex / 36 f) subjected to false twisting were further subjected to additional twisting by 600 turn / m and then woven at a weaving density of 82 yarns / inch (warp)×76 yarns / inch (weft), to obtain a woven fabric C having a mass per unit area of 70 g / m2, a thickness of 0.17 mm and an apparent density of 0.412 g / cm3.
production example 3
Production of Water-Soluble, Thermoplastic Polyvinyl Alcohol
[0046]A 100-L pressure reactor equipped with a stirrer, a nitrogen inlet, an ethylene inlet and an initiator inlet was charged with 29.0 kg of vinyl acetate and 31.0 kg of methanol. After raising the temperature to 60° C., the reaction system was purged with nitrogen by bubbling nitrogen for 30 min. Then, ethylene was introduced so as to adjust the pressure of the reactor to 5.9 kgf / cm2. A 2.8 g / L methanol solution of 2,2′-azobis(4-methoxy-2,4-dimethylvaleronitrile) was purged with nitrogen by nitrogen gas babbling. After adjusting the temperature of reactor to 60° C., 170 mL of the initiator solution was added to initiate the polymerization. During the polymerization, the pressure of reactor was maintained at 5.9 kgf / cm2 by introducing ethylene, the polymerization temperature was maintained at 60° C., and the initiator solution was continuously added at a rate of 610 mL / h. When the conversion of polymerization reached 70% ...
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