A kind of technology of continuous production polyisobutylene amine
A polyisobutylene amine and polyisobutylene technology, which is applied in the chemical industry, can solve the problems of high technical requirements of process equipment, difficult process technology control, difficult product step-by-step amplification, etc., so as to reduce the content of by-product impurities, reduce production costs, The effect of superior mass transfer and mixing performance
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Embodiment 1
[0033] In this embodiment, No. 1 microtubular reactor and No. 2 microtubular reactor are all tubular, and the insides are all filled with packing tubes. The equivalent diameter of No. 1 microtubular reactor and No. 2 microtubular reactor Both are 1mm.
[0034] The active polyisobutene is mixed with the solvent n-heptane and the catalyst acetic acid in a mass ratio of 10:5:3 to form an epoxidation raw material.
[0035] Send the epoxidation raw material and the hydrogen peroxide solution with a concentration of 30% into No. 1 microtubular reactor at the same time to carry out the epoxidation reaction, wherein the flow rate of the epoxidation raw material is 6ml / min, and the flow rate of the hydrogen peroxide solution is 7ml / min, the temperature of the epoxidation reaction is 85 ℃, and the pressure is 1.5MP, and the residence time of the reaction mixture in No. 1 microtubular reactor is 8min, and the crude product (epoxy polyisobutylene crude product) is obtained after the reac...
Embodiment 2
[0039] In this embodiment, No. 1 microtubular reactor and No. 2 microtubular reactor are all tubular, and the insides are all filled with static mixers. Wherein, the equivalent diameter of No. 1 microtubular reactor is 5 mm, and No. 2 microtubular reactor The equivalent diameter of the microtubular reactor is 2mm.
[0040] The active polyisobutene is mixed with the solvent n-octane and the catalyst acetic anhydride in a mass ratio of 10:5:3 to form an epoxidation raw material.
[0041] Send the epoxidation raw material and the hydrogen peroxide solution with a concentration of 30% into No. 1 microtubular reactor at the same time to carry out the epoxidation reaction, wherein the flow rate of the epoxidation raw material is 6ml / min, and the flow rate of the hydrogen peroxide solution is 8ml / min, the temperature of the epoxidation reaction is 95°C, the pressure is 1.8Mp, the residence time of the reaction mixture in No. 1 microtubular reactor is 10min, and the crude product (ep...
Embodiment 3
[0045] In this embodiment, No. 1 microtubular reactor and No. 2 microtubular reactor are both tubular, and filled with packing tubes inside, wherein, the equivalent diameter of No. 1 microtubular reactor is 1mm, and No. 2 microtubular reactor The equivalent diameter of the tubular reactor is 5 mm.
[0046] The active polyisobutene is mixed with the solvent n-heptane and the catalyst acetic acid in a mass ratio of 10:5:3 to form an epoxidation raw material.
[0047] Send the epoxidation raw material and the hydrogen peroxide solution with a concentration of 30% into No. 1 microtubular reactor at the same time to carry out the epoxidation reaction, wherein the flow rate of the epoxidation raw material is 10ml / min, and the flow rate of the hydrogen peroxide solution is 15ml / min, the reaction temperature of the epoxidation reaction is 75°C, the pressure is 1.6Mp, and the residence time of the reaction mixture in No. 1 microtubular reactor is 8min. After the reaction, the crude p...
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