Polyurethane resin slurry for leather and preparation method thereof
A polyurethane resin and slurry technology, applied in textiles, papermaking, fiber processing, etc., can solve the problems of aging, breakage and discoloration of synthetic leather parts, and achieve the effect of improving adhesion resistance, strength and heat resistance.
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Embodiment 1
[0030] Production of polyester polyol A: under nitrogen protection, adipic acid, ethylene glycol, and hydroxyethylated bisphenol A are added to the reaction vessel, wherein: the total molar weight of ethylene glycol and hydroxyethylated bisphenol A The molar ratio of adipic acid to adipic acid is 1.21:1, and the molar ratio of ethylene glycol to hydroxyethylated bisphenol A is 5:1. After adding 0.003% tetraisopropyl titanate catalyst, carry out transesterification reaction at normal pressure , gradually raise the reaction temperature to 200°C according to the amount of distilled water;
[0031] Add 0.03% triphenyl phosphite to start compression polymerization under reduced pressure, control the temperature at 220°C and gradually increase the vacuum degree to -0.085MPa, keep the reduced pressure reaction until the hydroxyl value test is qualified, and obtain the polyester polyol A with a hydroxyl value of 56.1.
[0032] Polyurethane resin slurry for microfiber synthetic leather...
Embodiment 2
[0035] Production of polyester polyol A: under nitrogen protection, adipic acid, ethylene glycol, and hydroxyethylated bisphenol A are added to the reaction vessel, wherein: the total molar weight of ethylene glycol and hydroxyethylated bisphenol A The molar ratio of adipic acid to adipic acid is 1.09:1, and the molar ratio of ethylene glycol to hydroxyethylated bisphenol A is 10:1. After adding 0.006% tetrabutyl titanate catalyst, carry out normal pressure transesterification reaction, according to The amount of distilled water gradually raised the reaction temperature to 220°C;
[0036] Add 0.1% triphenyl phosphite to start compression polymerization under reduced pressure, control the temperature at 245°C and gradually increase the vacuum degree to -0.085 MPa, keep the reduced pressure reaction until the hydroxyl value test is qualified, and obtain the polyester polyol A with a hydroxyl value of 56.1.
[0037] Polyurethane resin slurry for superfine fiber synthetic leather,...
Embodiment 3
[0040]Production of polyester polyol A: under nitrogen protection, adipic acid, ethylene glycol, and hydroxyethylated bisphenol A are added to the reaction vessel, wherein: the total molar weight of ethylene glycol and hydroxyethylated bisphenol A The molar ratio of adipic acid to adipic acid is 1.05:1, and the molar ratio of ethylene glycol to hydroxyethylated bisphenol A is 20:1. After adding 0.005% dibutyltin dilaurate catalyst, carry out normal pressure transesterification reaction, according to The amount of distilled water gradually raised the reaction temperature to 220°C;
[0041] Add 0.15% triphenyl phosphite to start decompression polymerization, control the temperature at 245°C and gradually increase the vacuum degree to -0.085MPa, keep the decompression reaction until the hydroxyl value test passes, and the polyester polyol A has a hydroxyl value of 56.1.
[0042] Polyurethane resin slurry for superfine fiber synthetic leather, including the following raw material ...
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