The utility model discloses a production device of polymeric
ferric chloride sulfate, which comprises a pressure-resistant tank body, a main / auxiliary liquid inlet
pipe orifice, an
exhaust pipe orifice and an upper gas inlet
pipe orifice are arranged at the top of the pressure-resistant tank body, a liquid outlet
pipe orifice is arranged at the bottom of the pressure-resistant tank body, and three lower gas inlet pipe orifices are uniformly distributed in the circumferential direction of the tank body; the main ejector is connected with a main liquid inlet pipe opening and exhausts circularly, and the auxiliary ejector injects liquid into the position below the liquid level through an extension pipe. According to the utility model, the design of an under-
liquid gas distribution pipe is canceled, and a three-dimensional
gas supply layout is adopted, so that the problems that the traditional structure is easy to corrode and perforate and the gas distribution is non-uniform are solved; the lower gas inlet pipe opening and the upper gas inlet pipe opening which are circumferentially symmetrical form a spiral gas-liquid
mixed flow, the gas
diffusion uniformity is improved, and oxidation dead angles are reduced; the main ejector and the auxiliary ejector work cooperatively, the long
throat structure of the main ejector strengthens turbulent mixing, the short
throat design of the auxiliary ejector generates deep
microbubbles, the gas-liquid contact area is increased, and the reaction efficiency is improved; the
oxygen distribution proportion and the injection mode can be flexibly adjusted to adapt to the
raw material concentration fluctuation of + / -20%.