Liquid phase impinging stream reactor with controllable acidity
A technology of impinging flow reaction and reaction device, applied in chemical/physical/physical-chemical stationary reactors, etc., can solve problems such as unfavorable unloading and cleaning, vibration of propeller and motor shaft, unsuitable for long-term operation, etc. Guarantee the effect of continuous and stable operation, large circulation volume and simple structure
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Embodiment 1
[0029]The acidity-controllable liquid-phase impingement flow reaction device has a horizontal reactor structure, including a reactor shell 11, which is jacketed, which is convenient for heating or cooling. In the middle of the left and right sides of the reactor shell 11, two coaxial variable-diameter guide tubes 8 are symmetrically installed respectively. There is enough space between the entrance of the guide tube 8 and the inner wall of the reaction shell 11 to be used as a material circulation flow channel, and a propulsive three-blade stirrer 7 and two stirrers 7 are respectively installed at the feed end of the guide tube 8 Coaxial symmetry, used to accelerate the fluid. An elbow feeding pipe 5 is arranged at the entrance of the diversion cylinder 8, and raw materials are input through the feeding pipe 5 with an elbow, which can be fed on one side or on both sides. Two feeding pipes 5 facilitate the feeding of two different reactants. Each feed pipe 5 is connected to a ...
Embodiment 2
[0032] The reaction device is the same as in Example 1.
[0033] Fill the reactor with deionized water, turn on the heat carrier circulation switch, conduct a constant temperature water bath through the jacket of the reactor shell and set the temperature to 60°C, turn on the speed controller 1 to make the motor 9 drive the agitator 7, and adjust the speed to 2000r·min -1 , after the temperature of the working medium in the reactor reaches 60°C, the mixed solution of ferric nitrate and phosphoric acid is fed by a metering pump at 0.1L·min -1 The flow rate is input into the reactor through the feeding pipe with a curved mouth on one side, and the concentrations of ferric nitrate and phosphoric acid in the mixed solution are both 0.1mol L -1 , while inputting 0.2mol·L through another elbow feeding tube -1 The pH value of the reaction system is controlled by the ammonia solution to be 2.3. After the process is stable, the products at 3 outlets of the reactor are collected, and t...
Embodiment 3
[0035] The reaction device is the same as in Example 1. Fill the reactor with deionized water, turn on the heat carrier circulation switch, conduct a constant temperature water bath through the jacket of the reactor shell and set the temperature to 50°C, turn on the speed controller 1 to make the motor 9 drive the agitator 7, and adjust the speed to 2900r·min -1 , after the temperature of the working medium in the reactor reaches 50°C, use a metering pump to increase the concentration to 0.1mol·L -1 The mixed solution of ferrous nitrate and phosphoric acid was added at 0.1L·min -1 The flow rate is input into the reactor through one elbow feeding tube, and at the same time, 4mol L is input through the other elbow feeding tube -1 The ammonia solution controls the pH value of the reaction system to 4.5, collects the product at the outlet of the reactor after the process is stable, and obtains spherical nano-scale iron phosphate after post-treatment procedures such as filtration...
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