A method of enhancing fluid mixing in a microreactor
A technology of fluid mixing and micro-reactor, which is applied in the fields of ultrasonic application, chemical equipment, and chemical strengthening methods. It can solve the problems that the ultrasonic strengthening effect is difficult to run stably for a long time, the ultrasonic strengthening effect is poor, and the processing cost is high. Two-phase mixing effect, prevention and dredging of clogging, effect of simple microchannel structure
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Embodiment 1
[0027] Embodiment 1, the mixing process of the bubbly flowing fluid is strengthened
[0028] In this embodiment, the continuous introduction of bubbly flow bubbles into a microreactor to enhance fluid mixing is taken as an example. In order to observe the effect of ultrasonically enhanced mixing, deionized water and a solution made of deionized water and ink were respectively passed into the two liquid inlet channels 1 and 2 of the microchannel, and the flow rate was 5ml / min; in the gas inlet channel 3 Into the air, the flow rate is 1ml / min such as figure 2 As shown, the injected air forms a bubble-like flow in the main channel 4, and the lateral size of the bubbles is about 300 μm. Without ultrasound, the ink and water flow along both sides of channel 4 and mix poorly. When 20 kHz is applied in the microreactor, the sound intensity is 1.5W / cm 2 After the ultrasonic wave, that is, the product of the ultrasonic frequency f and the gas phase transverse equivalent diameter d ...
Embodiment 2
[0029] Embodiment 2, Slug flow fluid mixing process strengthening
[0030] In this embodiment, the continuous introduction of slug-like air bubbles into the microreactor to enhance fluid mixing is taken as an example. In the two liquid inlet channels 2 and 1 of the microchannel, the deionized water and the solution made of deionized water and ink are respectively introduced, and the flow rate is 1ml / min; the air is introduced into the gas inlet channel 3, and the flow rate is 2ml / min. like Figure 4 As shown, the injected air forms a slug flow in the main channel 4, and the lateral size of the bubbles is about 1000 μm. Without ultrasound, the ink and water flow along both sides of channel 4 and mix poorly. When ultrasound is applied in the microreactor, the mixing effect of water and ink in channel 4 is significantly enhanced, see Figure 5 . Figure 5 Ultrasonic frequency 18 kHz, sound intensity 1.5W / cm 2 When the mixing effect of water and ink, the product of ultrason...
Embodiment 3
[0031] Embodiment 3, liquid-liquid precipitation reaction process strengthening
[0032] In this embodiment, bubble-like flow bubbles are continuously introduced into the microreactor through the gas inlet to prevent and clear microchannel blockage. The two liquid inlet channels 1 and 2 of the microchannel are respectively fed with a zinc nitrate solution and a sodium carbonate solution, and the two solutions enter the main channel 4 and then mix and react to form zinc carbonate solid particles. The flow of zinc nitrate solution and sodium carbonate solution is 50ml / min, and the concentration is 0.5mol / L; in the gas inlet channel 3, the air flow rate is 10ml / min, and the air that is introduced forms bubbles in the main channel 4 Shaped flow, the lateral size of the bubbles is about 300 μm. Image 6 It is the curve of the pressure drop with time when the reactor is running. When no ultrasound is applied, the zinc carbonate solid particles generated in the microchannel 4 are d...
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