Method of distilling liquid containing easily polymerizable compound
A distillation method and compound technology, applied in the field of distillation, can solve problems such as unfavorable economy, and achieve the effect of inhibiting polymerization
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[0057] Hereinafter, the present invention will be described in more detail by way of production examples, examples and comparative examples, but the present invention is not limited to these examples.
manufacture example
[0059] A distillation device made of SUS316 with a capacity of 2000L (simple distillation form. A multi-tube reboiler is set as a heating source, and a circulation pump is used for forced circulation.) is evacuated until the internal pressure reaches 5.33hPa, and then 1150kg (93.5% by mass) is fed ) a liquid containing hydroxyethyl methacrylate (hereinafter referred to as "HEMA") obtained from the reaction of methacrylic acid and ethylene oxide, and 0.12kg of p-methoxyphenol and 0.20kg of phenothiazine as polymerization inhibitors , steam was passed into the reboiler, and the distillation of the above-mentioned HEMA-containing liquid was started.
[0060] Distillation started when the liquid temperature reached 70°C, and was kept constant at 85°C thereafter. Distillation was terminated when the distilled amount reached 980 kg (85.2% by mass of the initial feed liquid), and 170 kg of distillation tower bottom liquid was obtained. Thereafter, the entire amount of the obtained d...
Embodiment 1
[0062] (first distillation)
[0063] In the same distillation apparatus as in the production example, feed 1150 kg of HEMA-containing liquid obtained by the reaction of methacrylic acid and ethylene oxide and 0.12 kg of p-methoxyphenol and 0.20 kg of phenothiene as a polymerization inhibitor. Zinc, start distillation.
[0064] From the moment when the amount of distillate reached 810 kg (70.4% by mass of the initial feed liquid), 62 kg (5.4% by mass of the initial feed liquid) of the distillation bottom liquid obtained in the production example was supplied to the distillation apparatus using a liquid delivery pump, Continue to distill. After 3.5 hours from the start of distillation, distillation was stopped when the amount of distillate reached 1100 kg (95.7% by mass of the initial feed liquid).
[0065] After the distillation was completed, 112 kg of residual tower bottom liquid remaining in the distillation apparatus was transferred to the same waste oil storage tank as i...
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