Suspension bed inorganic film reactor
An inorganic membrane and reactor technology, applied in the field of suspended bed inorganic membrane reactors, can solve the problem of not being used as a reactor, and achieve the effects of full reaction, reduced equipment investment and operating costs, and reduced membrane area.
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Embodiment 1
[0020] Such as figure 1 As shown, the reactor is composed of a stainless steel membrane tube with an average pore diameter of 200nm, and the space inside the inorganic membrane tube 5 is the reaction space. Taking the ammoxidation of acetone catalyzed by TS-1 to generate acetone oxime as an example, put acetone, solvent tert-butanol, catalyst TS-1 and magnetic stirring rotor into reactor 5 before the reaction, turn on the condensate water, and turn on the magnetic stirring device , heat up, when the reaction temperature reaches 70°C, start the constant flow pumps 3 and 9 at the same time, wherein the constant flow pump 3 adds ammonia to the reaction system, and the constant flow pump 9 adds acetone, hydrogen peroxide and solvent tert-butyl to the reaction system Alcohol mixed solution, the total feed rate is 0.43mL / min, and the vacuum suction pump 7 for discharging is turned on at the same time to start continuous discharge, and the discharge rate is 0.43mL / min. The reaction ...
Embodiment 2
[0022] Such as image 3 As shown, the reactor is composed of a zirconia membrane tube with an average pore diameter of 200nm, and the space inside the inorganic membrane tube 5 is the reaction space. Take the reaction of TS-1 catalyzing the ammoxidation of acetone to generate acetone oxime as an example, put acetone, solvent tert-butanol, and catalyst TS-1 into the reactor 5 before the reaction, turn on the condensate water, start the peristaltic pump 13 cycles, and raise the temperature at the same time , when the reaction temperature reaches 70°C, start the constant flow pumps 3 and 9 at the same time, wherein the constant flow pump 3 adds ammonia to the reaction system, and the constant flow pump 9 adds acetone, hydrogen peroxide and solvent tert-butanol to the reaction system to mix Liquid, the total feed rate is 0.43mL / min, while the vacuum suction pump 7 for discharging is turned on to discharge continuously, and the discharge rate is 0.43mL / min. The reaction is carried...
Embodiment 3
[0024] Such as Figure 4 As shown, the reactor is composed of three zirconia membrane tubes with an average pore diameter of 50 nm, and the space inside the inorganic membrane tube 5 is the reaction space. Take the reaction of TS-1 catalyzing the ammoxidation of acetone to generate acetone oxime as an example, put acetone, solvent tert-butanol, and catalyst TS-1 into the reactor 5 before the reaction, turn on the condensate water, start the peristaltic pump 13 cycles, and raise the temperature at the same time , when the reaction temperature reaches 70°C, start the constant flow pumps 3 and 9 at the same time, wherein the constant flow pump 3 adds ammonia to the reaction system, and the constant flow pump 9 adds acetone, hydrogen peroxide and solvent tert-butanol to the reaction system to mix Liquid, the total feed rate is 1.29mL / min, and the vacuum suction pump 7 for discharging is turned on to discharge continuously at the same time, and the discharge rate is 1.29mL / min. Th...
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