Single reflection hypergravity device and process for continuous preparation of toluene diisocyanate
A toluene diisocyanate and supergravity technology, applied in the field of single reflection supergravity devices, can solve the problems of poor reaction selectivity, decreased conversion rate, large difference in material volume flow ratio, etc., to avoid clogging and prevent urea substances. generated effect
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[0065] Example 1:
[0066] In a TDI manufacturer, the process and device of the present invention are used to carry out a pilot test. Specifically, the light solvent of o-dichlorobenzene is used as the inert solvent, and the temperature of the inert solvent solution of toluene diamine is 110° C., the mass fraction is 40%, and the mass flow rate is 110°C. is 1000Kg / h; the temperature of the phosgene inert solvent solution is 70°C, the mass fraction concentration of phosgene is 20%, the mass flow rate is 15240kg / h, and the volume flow ratio of phosgene and toluenediamine inert solution is approximately 15:1. The reactor reacts with a rotating packed bed type supergravity structure, and the packing is a wire mesh packing; the diameter of the casing is d 2 200mm, casing diameter d 2 with the main feed pipe diameter d 3 With a ratio of 2, the diameter of the main feed pipe is d 3 100mm; sleeve length L 1 with casing diameter d 2 The ratio is 10, the sleeve length L 1 is 2000...
Example Embodiment
[0069] Embodiment 2:
[0070] In a TDI manufacturer, the process and device of the present invention were used to carry out a pilot test. Specifically, the light solvent of o-dichlorobenzene was used as the inert solvent. The temperature of the phosgene inert solvent solution is 110℃, the mass fraction concentration of phosgene is 50%, and the mass flow rate is 9500kg / h. The approximate volume flow ratio of phosgene and toluenediamine inert solution is 1:1, and it enters the cold reactor for reaction. It adopts a stator-rotor type supergravity structure, and the filler is metal foam filler; the diameter of the casing is d 2 200mm, casing diameter d 2 with the main feed pipe diameter d 3 With a ratio of 10, the diameter of the main feed pipe is d 3 20mm; sleeve length L 1 with casing diameter d 2 The ratio is 1, the sleeve length L 1 is 200mm; the inner diameter d of the main feeding pipe 3 and nozzle outlet hole diameter D 2 The ratio is 1, and the diameter of the nozz...
Example Embodiment
[0072] Embodiment three:
[0073] In a TDI manufacturer, the process and device of the present invention are used to carry out a pilot test. Specifically, the light solvent of o-dichlorobenzene is used as the inert solvent. The temperature of the inert solvent solution of toluenediamine is 140°C, the mass fraction is 40%, and the mass flow rate is 140°C. is 3020kg / h; the temperature of the phosgene inert solvent solution is 100℃, the mass fraction concentration of phosgene is 30%, and the mass flow rate is 10820kg / h. The volume flow ratio of phosgene and toluenediamine inert solution is approximately 3:1, and the reaction is carried out in the cold reactor, using a spiral channel type supergravity structure, and the filler is a metal foam filler; it is characterized in that the diameter of the casing is d 2 150mm, casing diameter d 2 with the main feed pipe diameter d 3 With a ratio of 3, the diameter of the main feed pipe is d 3 50mm; sleeve length L 1 with casing diamete...
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