Polyisocyanate composition with long-term storage stability and preparation method thereof
A polyisocyanate, storage stability technology, applied in the direction of coating, can solve the problem of lack of research reports and effective solutions, affecting the downstream application of products, etc., to achieve the effect of improving storage stability
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Embodiment 1
[0058] 500 g of TDI 80 were weighed in a round bottom flask, preheated to 60°C and kept stirring. Then, polyols, 67 g of trimethylolpropane, 22 g of 1,4-butanediol, and 19 g of 1,2-propanediol, were simultaneously added thereto, and the reaction temperature was controlled to be 60° C., and the reaction was continued for 3 hours. When the mass percentage of NCO was detected to be 16-18%, 4.2 g of absolute ethanol (r=0.037) was added, and the reaction was continued for 2 hours, and the reaction temperature was controlled to be 60° C. to obtain a pre-product. The pre-product is separated and processed by a secondary thin film evaporator to separate excess monomers. The operating conditions are: the feed temperature is 80°C, the feed rate is 1kg / h, the primary separation temperature is 165°C, and the primary absolute pressure is 125Pa , the secondary separation temperature is 165°C, and the secondary absolute pressure is 3Pa. The secondary heavy components are collected, and ethy...
Embodiment 2
[0060] 500 g of TDI 80 were weighed in a round bottom flask, preheated to 60°C and kept stirring. Then, polyols, 67 g of trimethylolpropane, 22 g of 1,4-butanediol, and 19 g of 1,2-propanediol, were simultaneously added thereto, and the reaction temperature was controlled to be 40° C., and the reaction was continued for 3 hours. When the mass percentage content of NCO was detected to be 16-18%, 10.2 g of absolute ethanol (r=0.089) was added, and the reaction was continued for 2 hours, and the reaction temperature was controlled to be 70° C. to obtain a pre-product. The pre-product is separated and processed by a secondary thin film evaporator to separate excess monomers. The operating conditions are: the feed temperature is 80°C, the feed rate is 1kg / h, the primary separation temperature is 165°C, and the primary absolute pressure is 125Pa , the secondary separation temperature is 165°C, and the secondary absolute pressure is 3Pa. The secondary heavy components are collected,...
Embodiment 3
[0062] 500 g of TDI 80 were weighed in a round bottom flask, preheated to 60°C and kept stirring. Then, polyols, 67 g of trimethylolpropane, 22 g of 1,4-butanediol, and 19 g of 1,2-propanediol, were simultaneously added thereto, and the reaction temperature was controlled at 80° C., and the reaction was continued for 3 hours. When the mass percent content of NCO was detected to be 16-18%, 0.42 g of absolute ethanol (r=0.0037) was added, and the reaction was continued for 2 hours, and the reaction temperature was controlled to be 40° C. to obtain a pre-product. The pre-product is separated and processed by a secondary thin film evaporator to separate excess monomers. The operating conditions are: the feed temperature is 80°C, the feed rate is 1kg / h, the primary separation temperature is 165°C, and the primary absolute pressure is 125Pa , the secondary separation temperature is 165°C, and the secondary absolute pressure is 3Pa. The secondary heavy components are collected, and ...
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