Method used for extracting high purity methyl acetate from effluent of terephthalic acid industrial production
A methyl acetate, high-purity technology, applied in the field of extracting high-purity methyl acetate, can solve problems such as complex processes, and achieve the effect of simple process, simple steps, and no waste water discharge
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Embodiment 1
[0030] Embodiment 1, about 90% of the methyl acetate raw material is sent to the B1 side stream discharge rectification tower, the temperature of the control tower still is 63 ° C, the reflux ratio is 15, and the steam at the boiling point of 56 ~ 58 ° C is extracted from the side line, and the steam Directly sent to the B3 extractive distillation tower for extraction and rectification; the top of the tower is the light impurities in the raw materials, and the heavy components in the tower still enter the B2 recovery tower to recover the steam rich in methyl acetate, and the tower still gets the heavy impurities in the raw materials, and the tower top It is the steam rich in methyl acetate, which is sent to the raw material for recycling. The methyl acetate steam F of side line extraction and the saline extraction agent S that prepares are with the ratio of volume 1:1 (wherein, extraction agent S is dimethyl phthalate, and sodium bicarbonate accounts for 8wt of extraction agent...
Embodiment 2
[0036] The operation is basically the same as that of Example 1, except that the temperature of the bottom of the rectifying tower with single-side discharge is 70°C, and the reflux ratio is 15; the volume ratio of dimethyl sulfoxide and dimethyl phthalate in the extractant S is 2:1, the feed volume ratio of the methyl acetate steam F and the extractant S extracted from the side line is 1:2, and the purity of the high-purity methyl acetate P obtained at the top sampling port of the extractive distillation column B3 is 99.65% , the recovery rate of methyl acetate was 98.5%.
Embodiment 3
[0038] The operation is basically the same as in Example 1, except that the temperature of the rectification tower bottom of the single-side discharge rectification tower is 60 ° C, and the reflux ratio is 12; the volume ratio of dimethyl sulfoxide and dimethyl phthalate in the extractant S is 1 : 1, magnesium chloride accounts for 7wt% of extractant gross mass. The purity of the high-purity methyl acetate P obtained from the top sampling port of the extractive distillation column B3 is 99.60%, and the recovery rate of methyl acetate is 97.5%.
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