Rapid mold stripping urethane elastomer compoistion and use method thereof
A polyurethane elastomer and composition technology, applied in the field of castable polyurethane elastomer, can solve the problems of low TDI saturated vapor pressure, environmental hazards, long demoulding time, etc., achieve high saturated vapor pressure, reduce energy consumption, and excellent mechanics performance effect
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Embodiment 1
[0023] (1) Polymer components: 30% of polyether polyol (PPG1000) with a functionality of 2 and a molecular weight of 1000 and 34% of a polyether polyol (PPG3600) with a functionality of 3 and a molecular weight of 6000, 3,3'-dichloro- 35% of 4,4'-diaminodiphenylmethane (MOCA), 1% of organic bismuth catalyst and dehydration at 100-110°C and -0.095MPa until the water content is less than 0.05%, to obtain a polymer component.
[0024] (2) Prepolymer component: 45% polyether polyol (PPG1000) with 2 functionalities and a molecular weight of 1000, and 55% diphenylmethane diisocyanate MDI-505% are reacted at 70°C to 90°C for 2 hours to obtain isocyanate Prepolymer with 15% acid group content.
[0025] (3) Reaction part (during product production): Mix the prepolymer component and the polymer component at a ratio of 1:1, and the mixing temperature is 30°C. Then pouring and vulcanization molding (vulcanization at 70° C. to 80° C.) according to the usual method, mold opening after 10 m...
Embodiment 2
[0027] (1) Polymer component: 30.5% of polyether polyol (PPG2000) with functionality 2 and molecular weight 2000 and polyether polyol (PPG3600) with functionality 3 and molecular weight 6000 39, 3,3'-dichloro-4 , 30% of 4′-diaminodiphenylmethane (MOCA) and 0.5% of organic mercury catalyst are dehydrated at 100-110°C and -0.095MPa until the water content is less than 0.05%, to obtain a polymer component.
[0028] (2) Prepolymer component: 54.5% of polyether polyol (PPG-2000) with 2 functionalities and molecular weight of 2000, diphenylmethane diisocyanate MDI-10020% and MDI-5025.5% at 70°C to 90°C °C for 2 hours to obtain a prepolymer with an isocyanate content of 13%.
[0029] (3) Reaction part (during product production): Mix the prepolymer component and the polymer component at a ratio of 1:1, and the mixing temperature is 30°C. Then pouring and vulcanization molding (vulcanization at 70° C. to 80° C.) according to the usual method, mold opening after 10 minutes, and post-v...
Embodiment 3
[0031] (1) Polymer components: polyether polyol (PPG1000) 20 with functionality 2 and molecular weight 1000 and polyether polyol (PPG3600) 59 with functionality 3 and molecular weight 6000, 3,3'-dichloro-4, 20% of 4'-diaminodiphenylmethane (MOCA) and 1% of organic lead catalyst are dehydrated at 100-110°C and -0.095MPa until the water content is less than 0.05%, to obtain a polymer component.
[0032] (2) Prepolymer component: polyether polyol (PPG2000) with 2 functionalities and a molecular weight of 2000 (PPG2000) 63%, diphenylmethane diisocyanate MDI-5024%, liquefied MDI 13%, at 70°C to 90°C The reaction was carried out for 2 hours to obtain a prepolymer with an isocyanate content of 9%.
[0033] (3) Reaction part (during product production): Mix the prepolymer component and the polymer component at a ratio of 1:1, and the mixing temperature is 30°C. Then pouring and vulcanization molding (vulcanization at 70° C. to 80° C.) in the usual way, mold opening after 10 minutes, ...
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