Process for the purification of crude propene oxide
A technology of propylene oxide and compound, applied in the field of purification of crude propylene oxide, can solve the problems of inability to remove methanol, slow reaction and the like
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Embodiment 1
[0082] Crude propylene oxide comprising 52.7 wt. % propylene oxide, 44.3 wt. % methanol, 2.2 wt. % water, 1500 wppm acetaldehyde and 430 wppm methyl formate was subjected to continuous extractive distillation. The extractive distillation was carried out in a structured-packed column with a separation efficiency of 80 theoretical orders at a reflux ratio of 2 and operating at a pressure of 1.8 bar absolute. At stage 20 (counting from the bottom) 1241 g / h of crude propylene oxide was added. At the same time, 207 g / h of a 1.5% by weight aqueous solution of hydrazine were fed on stage 40 (counted from the bottom). At the top of the column, purified propylene oxide comprising 99.92% by weight of propylene oxide, 36 wppm of methanol, 70 wppm of water, less than 20 wppm of acetaldehyde and 390 wppm of methyl formate was extracted at a flow rate of 658 g / h.
Embodiment 2
[0084] Repeat Example 1, the difference is only in:
[0085] 1301 g / h of crude propylene oxide comprising 51.3% by weight of propylene oxide, 46.13% by weight of methanol, 2.0% by weight of water, 1200 wppm of acetaldehyde and 280 wppm of methyl formate were mixed with 80 g / h of 0.5% sodium hydroxide The aqueous solutions were mixed and the mixture was allowed to react in a tubular reactor at 60°C for 30 minutes before being added to the extraction column. The aqueous hydrazine solution was added at a lower flow rate of 100 g / h. At the top of the column, purified propylene oxide comprising 99.98% by weight of propylene oxide, 33 wppm of methanol, 50 wppm of water, 8 wppm of acetaldehyde and 52 wppm of methyl formate was extracted at a flow rate of 658 g / h.
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