Method for synthesizing, extracting and purifying 3-hexyne-2, 5-diol
A technology for hexynediol and hexyne, which is applied in the field of safe synthesis and separation and purification of 3-hexyne-2,5-diol, can solve problems such as difficulty in production, and achieve safe production, convenient transportation and storage, The effect of eliminating the explosion hazard
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Embodiment 1
[0043] (1) Distill paraldehyde through acid-catalyzed depolymerization, and absorb it with n-hexane solvent to make a solution with acetaldehyde content of 40.9%. Take 318g of the solution (equivalent to 130g of acetaldehyde), and seal it for use.
[0044] (2) Put 400g of n-hexane and 210g of potassium hydroxide (industrial grade, purity 94%) into the grinder in turn to grind into a slurry, transfer it to a stainless steel pressure reactor, start stirring, heat to 70°C-80°C and keep 1 hour, then lower the temperature to 18 ℃ ~ 20 ℃ control.
[0045] (3) Introduce acetylene gas and keep the acetylene pressure in the range of 0.08MPa-0.1MPa to react for about 1 hour. Then add the acetaldehyde solution prepared above into the reaction kettle evenly and slowly from the head tank, while keeping the acetylene pressure in the range of 0.08MPa-0.12MPa to react, and gradually increase it at a rate of 2°C-3°C every 10 minutes. Keep it after the high temperature reaches 54℃~56℃. After ...
Embodiment 2
[0053] Operate according to the mode of operation of embodiment 1, wherein:
[0054] The solvent used in the operation step (1) is petroleum ether, and the concentration of the prepared acetaldehyde solution is 38.1%. Weigh 368g of the solution (containing 140g of acetaldehyde) for use.
[0055] In the operation step (2), the feeding materials are 540g of solvent petroleum ether and 217g of catalyst potassium hydroxide.
[0056] In the operation step (3), the acetaldehyde: potassium hydroxide = 1.15: 1 (molar ratio) is controlled, and the acetylene pressure is 0.1MPa~0.12MPa.
[0057] The amount of clean water in the operation step (5) is 750g.
[0058] In the operation step (6), the extraction solvent is fed with 700 g of 2-ethylhexanol.
[0059] Rectification yielded 167.2 g of 3-hexyne-2,5-diol with a purity of 98.4%.
Embodiment 3
[0061] Operate according to the mode of operation of embodiment 1, wherein:
[0062] The solvent used in the operation step (1) is toluene, and the concentration of the prepared acetaldehyde solution is 42.7%. Weigh 305g of the solution (containing 130g of acetaldehyde) for use.
[0063] In the operation step (2), the feeding materials are 400 g of solvent toluene and 210 g of catalyst potassium hydroxide.
[0064] In the operation step (3), the acetaldehyde: potassium hydroxide = 1.22: 1 (molar ratio) is controlled, and the acetylene pressure is 0.12MPa~0.14MPa.
[0065] The amount of clean water in the operation step (5) is 700g.
[0066] The extraction solvent in the operation step (6) is 650 g of isobutanol.
[0067] Rectification yielded 157.7 g of 3-hexyne-2,5-diol with a purity of 97.8%.
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