A kind of preparation method of high-performance grinding aid monomer diisopropanol monoethanolamine
A technology of monoethanolamine and diisopropanol, which is applied in the preparation of organic compounds, chemical instruments and methods, and the preparation of aminohydroxyl compounds, etc., can solve the problem of the small amount of the target product of diisopropanol monoethanolamine, monoethanolamine and propylene oxide Difficult to control the polymerization rate, poor material mass transfer, poor heat transfer effect, etc., to achieve the effect of reducing the generation of a large number of by-products, good control, and good heat transfer effect
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Embodiment 1
[0016] Example 1: The preparation method of a high-performance grinding aid monomer diisopropanol monoethanolamine of this example, the steps are:
[0017] Adopt 2M 3 Press external circulation spray polymerization equipment, 815kg propylene oxide (PO) monomer is prepared in the metering tank. Turn on the vacuum system, and suck 427kg ethanolamine and 210kg deionized water into the kettle. After the completion, the reaction kettle is closed after the nitrogen is discharged three times. Start the canned motor pump, open the steam valve of the heat exchanger, and slowly increase the temperature. When the temperature in the kettle rises to about 50°C, PO is slowly added dropwise, and the temperature rises significantly. When the temperature rises to 65°C, the cooling water is turned on and the material is smoothly fed. Polymerization process: 0.06Mpa≤P≤0.21Mpa, 60℃≤T≤75℃, after feeding, mature for 1.0hr, slightly open the reactor vacuum system, the vacuum degree is -0.035~-0.075MPa,...
Embodiment 2
[0018] Example 2: The preparation method of a high-performance grinding aid monomer diisopropanol monoethanolamine of this example, the steps are:
[0019] Adopt 2M 3 Press external circulation spray polymerization reaction equipment, 850kg propylene oxide (PO) monomer is prepared in the metering tank. Turn on the vacuum system, suck in 430kg of monoethanolamine and 230kg of deionized water into the kettle, and close the reactor after exhausting nitrogen three times. Start the canned motor pump, open the steam valve of the heat exchanger, and slowly increase the temperature. When the temperature in the kettle rises to 55℃, the PO is slowly added dropwise, the temperature rises obviously, the cooling water is turned on, and the feed is smoothly fed. The entire polymerization process: 0.05Mpa≤P ≤0.19Mpa, 55℃≤T≤75℃, after the feeding is finished, mature for 1.5hr, slightly open the vacuum system of the reactor, and the vacuum degree is -0.029~-0.070MPa, and the residual unreacted PO...
Embodiment 3
[0020] Example 3: The preparation method of a high-performance grinding aid monomer diisopropanol monoethanolamine of this example, the steps are:
[0021] Use 10M 3 Press external circulation spray polymerization equipment, 4250kg propylene oxide (PO) monomer is prepared in the metering tank. Turn on the vacuum system, suck in 2150kg of monoethanolamine and 1150kg of deionized water into the kettle, and close the reactor after exhausting nitrogen three times. Start the canned motor pump, open the steam valve of the heat exchanger, and slowly increase the temperature. When the temperature in the kettle rises to 50℃, start to slowly add PO, the temperature rises, turn on the cooling water, and smoothly feed the entire polymerization process: 0.07Mpa≤P≤ 0.23Mpa, 50°C≤T≤70°C, after the feeding is finished, mature for 1.5hr, slightly open the vacuum system of the reactor, the vacuum degree is -0.035~-0.073MPa, and remove the residual unreacted PO under reduced pressure. After finish...
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