Chamois initation artificial leather and manufacturing method thereof
A technology of artificial leather and imitation suede, which is applied in the field of semi-silver surface style artificial leather and silver surface style artificial leather. there is a problem etc.
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[0135] The present invention will be specifically described below based on examples, but the present invention is not limited to these examples. "Parts" and "%" in the examples are "parts by mass" and "% by mass" unless otherwise specified.
[0136] [tensile strength]
[0137] According to 5.12.1 of JIS L1079, the tensile strength of a test piece having a width of 25 mm cut along the MD direction (longitudinal direction) and the CD direction (transverse direction) was measured, and expressed as the average value.
[0138] [tear strength]
[0139] In accordance with 5.14 of JIS L1079, the tear strength of a test piece having a width of 25 mm cut along the MD direction (longitudinal direction) and the CD direction (transverse direction) was measured and expressed as an average value.
[0140] [Light fastness]
[0141] Judgment using the faded gray grading card specified in JIS L0804 Irradiate the suede artificial leather surface with a xenon arc lamp for 100 hours (black plat...
manufacture example 1
[0165] Add 29.0kg of vinyl acetate and 31.0kg of methanol into a 100L pressurized reactor equipped with a stirrer, nitrogen inlet, ethylene inlet, and initiator addition inlet, and replace the reaction system with nitrogen by bubbling nitrogen for 30 minutes after heating up to 60°C . Then import ethylene to make the reactor pressure 5.9kg / cm 2 . Dissolve 2,2'-azobis(4-methoxy-2,4-dimethylvaleronitrile) (AMV) in methanol to prepare an initiator solution with a concentration of 2.8g / L, and perform nitrogen bubbling to replace nitrogen. After adjusting the temperature in the above-mentioned polymerization tank to 60° C., 170 ml of the above-mentioned initiator solution was injected to initiate polymerization. Introduce ethylene during polymerization to maintain the pressure of the reactor at 5.9kg / cm 2 , the polymerization temperature was 60° C., and the above-mentioned initiator solution was continuously added at 610 ml / hr to carry out polymerization. After 10 hours, when ...
Embodiment 1
[0169] Using ethylene 10 mol% modified PVA (fusing point 206° C.) obtained in Manufacturing Example 1 as a sea component, an intrinsic viscosity of 0.65 (equal mass mixed solution of phenol / tetrachloroethane) containing 2.0 mass % of carbon black at 30 ℃ measurement) polyethylene terephthalate chips containing 8 mol% of isophthalic acid (hereinafter also referred to as IPA) as the island component, the mass ratio of the island component and the sea component is 60:40, and the island component ratio is 36 The islands were discharged and spun at 240° C. from a nozzle for melt composite spinning. The spun fiber was drawn by a roller plate system under normal conditions to obtain a multifilament of 70 dtex / 24 filaments. Spinnability, continuous runnability, and draftability were good, and there were no particular problems. The obtained island-in-the-sea type microfiber-forming fibers were subjected to mechanical crimping, then cut into 51 mm, defibrated by a carding machine, and ...
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