The utility model provides a
continuous flow reactor for synthesis of tetrabutylurea, which comprises a reactor body, an upper
mixing zone, a
reaction zone and a lower
mixing zone are arranged in the reactor body in a separating manner, and the reactor body is provided with a tetrabutylurea
discharge port, a
phosgene feed port, a liquid caustic soda feed port and a di-n-
butylamine feed port. A gas distribution plate is arranged in the lower mixing area to divide the lower mixing area into a lower
material distribution area and a discharging area, annular
phosgene gas distribution pipes are distributed on the gas distribution plate, the
phosgene feeding port is connected with the phosgene gas distribution pipes, and a tetrabutyl
urea discharging channel is formed in the lower partition plate; phosgene one-way inlet valves are distributed on a bottom plate of the lower partition plate; a
material distribution plate is arranged in the upper mixing area to divide the upper mixing area into an upper
material distribution area and an upper mixing area, a liquid caustic soda material distribution pipeline and a di-n-
butylamine material distribution pipeline are distributed on the material distribution plate, and a plurality of
mixed feeding holes are distributed in an upper partition plate; the temperature rise of phosgene is converted into a
gas phase from a
liquid phase, the phosgene reacts with di-n-
butylamine, the di-n-butylamine moves from top to bottom, and the
continuous flow reaction can improve the
utilization rate of raw materials and increase the yield.