A kind of triethanolamine continuous production device and process
A technology of triethanolamine and ethanolamine, applied in organic chemistry, chemical/physical/physical chemical processes, chemical instruments and methods, etc., can solve the problems of low purity of triethanolamine, intermittent reaction, etc., shorten reaction time, reduce side reactions, The effect of improving the reaction selectivity
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Embodiment 1
[0058] like figure 1 As shown, the ethylene oxide gas is liquefied and added to the ethylene oxide storage tank V01 and the ethylene oxide storage tank IV03, and pressurized to 0.8MPa with nitrogen gas; quantitative water is put into the ammonia water storage tank V02, and the liquid ammonia is passed through Put the pressure into the ammonia water storage tank V02, react with water to prepare an ammonia solution with a concentration of 60%, pressurize it to 1.2MPa with nitrogen gas, and control ammonia / alkane (referring to NH 3 The molar ratio to ethylene oxide) is 3, fed by feed pump I P01 and feed pump II P02 respectively, the total flow rate of feed is 2.0L / h, microchannel heat exchanger E01, micro mixer MCR-1 And the temperature of the tube reactor ST-1 is set to 90 °C, the back pressure valve I BPV01 back pressure is 4.0MPa, the two feed liquids enter the micro-mixer MCR-1 to mix and further React for 10 minutes, the reaction liquid flows through the back pressure valve...
Embodiment 2
[0060] The device and process are the same as in Example 1, except that 80% ammonia water is prepared, the ammonia / alkane molar alkane ratio is 2, and the microchannel heat exchanger E01, micro-mixer MCR-1 and tubular reaction are used in the reaction of ethanolamine production. The temperature of the device ST-1 is set to 100 degrees, and the back pressure of the back pressure valve I BPV01 is 5.0 MPa; the obtained triethanolamine has a purity of 91%.
Embodiment 3
[0062] The device and process are the same as in Example 1, except that 95% ammonia water is prepared, the ammonia / alkane molar ratio is 1, and the microchannel heat exchanger E01, micromixer MCR-1 and shell-and-tube reactor are used in the reaction of ethanolamine production. The temperature of ST-1 is set at 120 degrees, and the back pressure valve I BPV01 back pressure is 6MPa; The temperature of the micro-mixer I MCR-2 and the tubular reactor I ST-2 in the production of triethanolamine is set at 50 degrees, and the obtained three The purity of ethanolamine is 90.3%.
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