Preparation method of 1-amino-2-propanol
A technology of propanol and amino, which is applied in the field of preparation of 1-amino-2-propanol, can solve the problem that the crude product has many by-products and cannot meet the technical requirements and yield of high-purity 1-amino-2-propanol Low-level problems, to achieve the effect of shortening the molecular diffusion time, reducing the thickness of the boundary layer, and improving mass transfer
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Embodiment 1
[0018] Propylene oxide and ammonia water with a concentration of 95wt% are input into the mixer with a metering pump at a molar ratio of 1:1.0, and the temperature in the mixer is controlled at 0°C and the pressure at 3.0MPa; the mixed solution is continuously fed into the microchannel for reaction In the reactor, the material reacts in the channel of the reaction section of the reactor. The temperature is 60°C and the pressure is 3.0MPa. The time is 2S, and the specific cooling rate is controlled at about 1800-2000°C / min. Then the low boilers were removed through a stripping tower to obtain the product 1-amino-2-propanol with a content of 99.2%. In this embodiment, the microchannel reactor is specifically made of stainless steel, wherein the inner diameter of the microchannel is 0.05 mm, and the length of the microchannel is 0.8 m.
Embodiment 2
[0020] Propylene oxide and ammonia water with a concentration of 95wt% are input into the mixer with a metering pump at a molar ratio of 1:1.05, and the temperature in the mixer is controlled to be 10°C and the pressure is 5.0MPa; the mixed solution is continuously passed into the microchannel for reaction In the reactor, the material reacts in the channel of the reaction section of the reactor at a temperature of 80°C and a pressure of 5.0MPa. After staying for 0.5S, the material enters the cooling section of the microchannel reactor and rapidly cools down to terminate the reaction. The outlet temperature is -5°C. The residence time is 3.0S, and the specific cooling rate is controlled at about 1600-1800°C / min. Then the low boilers are removed through a stripping tower to obtain the product 1-amino-2-propanol with a content of 99.0%. The microchannel reactor is specifically made of titanium alloy. The inner diameter of the microchannel is 0.10mm, and the length of the microch...
Embodiment 3
[0022] Propylene oxide and ammonia water with a concentration of 97wt% are input into the mixer with a metering pump at a molar ratio of 1:1.05, respectively, and the temperature in the mixer is controlled at -10°C and the pressure is 8.0MPa; the mixed solution is continuously passed into the microchannel In the reactor, the material reacts in the channel of the reaction section of the reactor at a temperature of 70°C and a pressure of 8.0MPa. After staying for 1.0S, it enters the cooling section of the microchannel reactor and rapidly cools down to terminate the reaction. The outlet temperature is 20°C. The residence time is 2.0S, and the specific cooling rate is controlled at about 1400-1500°C / min. Then the low boilers are removed through a stripping tower to obtain the product 1-amino-2-propanol with a content of 99.6%. The microchannel reactor is specifically made of Hastelloy alloy. The inner diameter of the microchannel is 0.3mm, and the length of the microchannel is 3m...
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