Production process for performing oxyalkylation on alkynol
A production process and oxygenation technology, which is applied in the production process field of alkoxylation of alkynols, can solve the problems of increased production cost, high requirements on reaction vessels, dangerous operators, etc., and achieves improved production efficiency and full controllability. , the effect of low reaction temperature
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Embodiment 1
[0032] Add 20% ethylene oxide to 2,4,7,9-tetramethyl-5-decyne-4,7-diol, the production process includes:
[0033] a. Use a pump to transport 4000kg of 2,4,7,9-tetramethyl-5-decyne-4,7-diol melted in advance at 55~65°C to the head tank for metering, and put it into a volume of 6m 3 In the sealed low-pressure reactor, the reactor is a standard reactor with heat transfer oil or steam heating on the outer coil, water cooling on the inner coil, and frame or paddle type stirring. Add the mixture of 24.6kg trimethylamine and 0.4kg potassium hydroxide through the feeding device on the reactor.
[0034] b. Add 1050kg of ethylene oxide into the reactor at a rate of 4-5kg / min through the ethylene oxide metering pump. During the addition process, control the temperature in the reactor at 50-55°C and the pressure not to exceed 0.35MPa. When the pressure exceeds 0.35MPa, suspend feeding, and continue feeding when the pressure is lower than 0.3MPa. After the feeding is completed, keep the ...
Embodiment 2
[0040] 2,5,8,11-Tetramethyl-6-dodeyn-5,8-diol is added with 30% ethylene oxide, the production process includes:
[0041] a. Use a pump to transport 3500kg of 2,5,8,11-tetramethyl-6-dodecanyne-5,8-diol melted at 65~70℃ in advance to the head tank for metering, then put it into a closed low-pressure reactor middle. Add the mixture of 29.85kg triethylamine, 0.06kg potassium hydroxide and 0.09kg aluminum trichloride through the feeding device on the reactor.
[0042] b. Add 1600kg of ethylene oxide into the reactor at a rate of 3-4kg / min through the ethylene oxide metering pump. During the addition, control the temperature in the reactor at 65-70°C and the pressure not to exceed 0.4MPa. When the pressure exceeds 0.4MPa, stop feeding, and when the pressure is lower than 0.35MPa, continue feeding. After the feeding is completed, keep the temperature for about 3 hours, and wait until the pressure in the kettle drops to no longer changes.
[0043] c. Cool down after the reaction, ...
Embodiment 3
[0048] 2,4,7,9-tetramethyl-5-decyne-4,7-diol is added with 20% ethylene oxide and 10% propylene oxide. The production process includes:
[0049] a. Use a pump to transport 3500kg of 2,4,7,9-tetramethyl-5-decyne-4,7-diol melted in advance at 55~60°C to the head tank for metering, then put it into a closed low-pressure reactor . Add the mixture of 16.5kg trimethylamine, 12.9kg triethylamine, 0.3kg potassium hydroxide, 0.3kg zinc chloride through the feeding device on the reaction kettle.
[0050] b. Add 1050kg of ethylene oxide and 550kg of propylene oxide into the reactor at a speed of 1.5-2kg / min through the ethylene oxide metering pump. More than 0.4MPa. When the pressure exceeds 0.4MPa, stop feeding, and when the pressure is lower than 0.35MPa, continue feeding. Keep the temperature for about 4 hours after the feeding is completed, and wait until the pressure in the kettle drops to no longer changes.
[0051] c. Cool down after the reaction, replace the remaining ethylen...
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