A kind of sucralose-6-ethyl ester purification method
A technology of sucralose and purification method, which is applied in the field of sugar industry, can solve the problems of affecting the quality of sucralose products, increasing the amount of solvent used, production and environmental burden, etc., achieve high industrial application value, and reduce the amount of solvent used , the effect of reducing the number of crystallization
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Embodiment 1
[0061] 1t sucralose-6-ethyl ester mother liquor with a water content of 30% was added to the mixing kettle E-1, and boiled at 40°C, specifically, adding 90% of the mother liquor quality water at a stirring speed of 300r / min, Stir well. After stirring for 0.5h, it is separated by the solid-liquid separator H-1, the solid is returned to the mixing kettle E-1, and the mother liquor enters the liquid phase separator E-2 to stand; The brown tar in the lower phase is removed, and the upper phase enters the upper edge of the extraction tower E-3; the extraction agent cyclopentane enters from the lower edge of the extraction tower E-3, the ratio of the two is 1:0.5, and the temperature is 30 °C. Extraction, after the extraction is completed, the sucralose-6-ethyl ester aqueous solution without white oil is extracted from the bottom of the tower, and the alkane mixed liquid is extracted from the top of the tower; the extracted liquid from the bottom of the extraction tower enters the e...
Embodiment 2
[0066] Add 2t sucralose-6-ethyl ester mother liquor with a water content of 40% into mixing kettle E-1, heat and boil at 90°C, add water with a mass of 80% of the mother liquor at a stirring speed of 400r / min, and stir well. After stirring for 0.5h, it is separated by the solid-liquid separator H-1, the solid is returned to the mixing kettle E-1, and the mother liquor enters the liquid phase separator E-2 to stand; The brown tar in the lower phase is removed, and the upper phase enters the upper edge of the extraction tower E-3; the extraction agent cyclohexane enters from the lower edge of the extraction tower, and the ratio of the two is 1:0.6. The sucralose-6-ethyl ester aqueous solution without white oil is extracted from the bottom, and the alkane mixed liquid is extracted from the top of the tower; the extracted liquid from the bottom of the extraction tower enters the evaporator E-4 for evaporation, and the obtained solid is passed through ethyl acetate twice. Cooling a...
Embodiment 3
[0070] The 3t sucralose-6-ethyl ester mother liquor with a water content of 50% was added to the mixing kettle E-1, heated and boiled at 55°C, and 65% of the mother liquor mass was added at a stirring rate of 250r / min, and stirred thoroughly. After stirring for 1.5h, it is separated by solid-liquid separator H-1, the solid is returned to mixing kettle E-1, and the mother liquor enters liquid phase separator E-2 to stand; The brown tar in the lower phase is removed, and the upper phase enters the upper edge of the extraction tower E-3; the extraction agent isoheptane enters from the lower edge of the extraction tower, and the ratio of the two is 1:0.8. The sucralose-6-ethyl ester aqueous solution without white oil is extracted from the bottom, and the alkane mixed liquid is extracted from the top of the tower; the extracted liquid from the bottom of the extraction tower enters the evaporator E-4 for evaporation, and the obtained solid is passed through ethyl acetate twice. Cool...
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