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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

Active Publication Date: 2014-11-26
TSINGHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Thirdly, the motor shaft driving the propeller is a cantilever structure. If the shaft is long or the speed is fast, it will easily cause vibration of the propeller and the motor shaft, and the deformation of the shaft will cause the motor to not work, which is not suitable for long-term operation.
In addition, there is a vortex flow in the fluid in the guide tube, and a vortex is generated in the flow, resulting in a large amount of energy loss
Finally, the bottom of the container is designed horizontally. For systems with solid particles or crystallization, it is not conducive to unloading and cleaning the container after the reaction.

Method used

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  • Liquid phase impinging stream reactor with controllable acidity
  • Liquid phase impinging stream reactor with controllable acidity
  • Liquid phase impinging stream reactor with controllable acidity

Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

The invention discloses a liquid phase impinging stream reactor with controllable acidity, belonging to the field of chemical reaction technical equipment. In the reactor, 1-6 pairs of draft tubes with changeable diameters are horizontally arranged coaxially and oppositely; raw materials are introduced by feeding tubes with curved nozzles; fluid is accelerated by push-type three-blade stirrers at the entrance of the draft tubes; the rotation speed of the push-type three-blade stirrers is controlled by a controller; rotational flow is inhibited by deflection baffles; the inner diameters of the draft tubes become smaller gradually; cross-section area of a flow channel is decreased; flow speed is increased; the flow speed at the exits of the draft tubes is the maximum; two fluids impinge face to face at a high speed in the container and mixed efficiently and rapidly; the fluids flow to the entrance of the draft tubes from central impinging areas through the outer sides of the draft tubes, thus realizing circulation; motors are fixed and anti-vibrated by triangle support plates, the acidity of a reaction system is on-site monitored by a pH meter probe and displayed in real time by a pH meter display; constant acidity of the reaction system is realized by adjusting liquid inlet flow quantity; and materials in the contained are discharged from a material-discharging port after the reaction is finished. The liquid phase impinging stream reactor can be heated or cooled, and can be operated continuously, intermittently or semi-continuously.

Description

technical field [0001] The invention belongs to the field of chemical reaction technical equipment, and relates to a liquid phase impingement flow reaction device with controllable acidity. Background technique [0002] In the engineering fields of chemical engineering, materials and pharmaceuticals, the process of preparing ultrafine powder by liquid phase reaction is often involved. The problem of rapid and uniform mixing of materials in the reaction device is the bottleneck of the quality of the product prepared in this process, which directly affects the particle size and particle size distribution of the product particles. . [0003] The traditional device widely used in the liquid phase reaction process in industry is the tank-type stirred tank reactor. This kind of reactor is usually in a container whose height is slightly larger than the diameter. Mixing occurs due to relative motion. Because the relative motion between flow groups produced in this way is not stron...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J19/18
Inventor 蒲薇华肖杨武玉玲邓长生
Owner TSINGHUA UNIV
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