Continuous-flow catalytic reactor and assembly method and application thereof
A technology of catalytic reactors and assembly methods, applied in chemical instruments and methods, chemical/physical/physicochemical processes of energy application, chemical/physical processes, etc., can solve the problem of loss of activity, limited catalyst life, and catalytic active components. Carrier limited binding force and other issues, to achieve the effect of improving utilization efficiency, saving separation steps, and promoting chemical reactions
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Embodiment 1
[0051] Embodiment 1: The structure of a kind of continuous flow catalytic reactor of this embodiment is as figure 1 shown. Among them, the reaction tube 1 is W-shaped, made of glass, with an inner diameter of 1.8 cm, a length of 70 cm, and a volume of 178 ml. The reaction tube 1 is filled with coconut shell activated carbon filler 2, the particle size is 12 to 30 mesh, and the mass is 80 grams. The two ends of the filler are respectively packaged with quartz wool 3 and 4; , seal and fix the graphite electrodes 11, 12 with silica gel plugs 9, 10; two electrodes go deep into the reaction tube 1 and short-circuit with the quartz wool 3, 4, and short-circuit with the negative pole of the DC power supply 13; open 14 in the middle of the reaction tube, The plug 15 seals and fixes the graphite electrode 16, and the electrode goes deep into the reaction tube 1 and short-circuits with the filler 2, and short-circuits with the positive pole of the DC power supply 13.
[0052] Prepare ...
Embodiment 2
[0053] Embodiment 2: In the reaction tube 1 described in Embodiment 1, fill the chlorine ion exchange resin filler 2, the particle size is 20~50 mesh, the mass is 100 grams, the two ends of the filler are respectively packaged with glass wool 3, 4, and the connection mode with the DC power supply With embodiment 1.
[0054] Prepare 400 ml of molybdic acid solution with a concentration of 0.2 g / L. Turn on the DC power supply 13 and keep the voltage at 10 volts. The solution is pumped into the reaction tube 1 from the liquid inlet at a flow rate of 2 ml / min, flows through the filler 2, and is pumped out from the liquid outlet 6, and the molybdate ions are electrosorbed in the On packing 2, a continuous flow catalytic reactor is obtained.
Embodiment 3
[0055] Embodiment 3: fill coconut shell activated carbon filler 2 in the reaction tube 1 described in embodiment 1, particle diameter 12~30 orders, quality 80 grams. Both ends of the filler are encapsulated with glass wool 3 and 4 respectively. The connection direction of the positive and negative poles of the DC power supply is opposite to that of Embodiment 1. The glass wool 3 and 4 at both ends of the filler are short-circuited to the positive pole of the power supply 13, and the middle part is short-circuited to the negative pole of the power supply 14.
[0056] Prepare 100 ml of ferric hydroxide sol with a concentration of 2 g / L. Turn on the DC power supply 13 and keep the voltage at 50 volts. The sol is pumped into the reaction tube 1 from the liquid inlet at a flow rate of 0.2 ml / min, flows through the filler 2, and is pumped out from the liquid outlet 6. The ferric hydroxide colloidal particles are charged by the electric Adsorption on packing 2 results in a continuou...
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Abstract
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