Method for producing light colored dicyclohexyl methane diisocyanate
A technology for dicyclohexylmethane and diisocyanate is applied in the field of preparing light-colored dicyclohexylmethane diisocyanate and can solve problems such as unfavorable downstream applications
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Embodiment 1
[0047] Embodiment 1: gas phase method prepares dicyclohexylmethane diisocyanate
[0048] The alcohol compound content is 0.05wt% H 12 MDA is gasified and heated to 355°C, mixed with nitrogen at 300°C, and gaseous phosgene heated to 355°C is continuously fed into the reactor through the respective feed pipes, under the conditions of absolute pressure 0.05MPa and temperature 360°C react below. where H 12 The feeding amount of MDA is 100Kg / h, and the feeding amount of phosgene is 300Kg / h. After the reaction, the mixed gas is rapidly cooled to 100°C-140°C with o-dichlorobenzene solution through a gas jet absorption device to obtain the product containing H 12 MDI actinic liquid, after further dephosgene, HCl, desolventization and distillation processes, pure H can be obtained 12 MDI products.
[0049] Embodiment 2-4 gas phase phosgenation reaction is carried out under the same conditions with embodiment 1, and difference is only that H 12 The content of alcohol compounds in ...
Embodiment 5
[0054] Embodiment 5: Preparation of dicyclohexylmethane diisocyanate by liquid phase method
[0055] The alcohol compound content is 0.05wt% H 12 MDA is configured into a 15% solution with chlorobenzene as a solvent, and is preheated to 40°C, and simultaneously passed into a reaction kettle containing chlorobenzene with liquid phosgene at -5°C for liquid-phase phosgenation reaction, wherein H 12 The feeding amount of MDA is 100Kg / h, the feeding amount of cold reaction phosgene is 1000kg / h, the cold reaction temperature is controlled at 60°C, and the residence time is 5min, and the thermal reaction temperature is controlled at 140°C, and the residence time is 2h, to obtain Contains product H 12 MDI actinic liquid, after further dephosgene, HCl, desolventization and distillation processes, pure H can be obtained 12 MDI products.
[0056] Embodiment 6-8 liquid phase phosgenation reaction is carried out under the same conditions, and the difference is only that H 12 The conten...
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