A method for synthesizing high-purity sucrose monoester
A sucrose monoester, high-purity technology, applied in the field of sucrose ester manufacturing, can solve the problems of low monoester content, difficult to remove, dark color, etc., to achieve the effect of preventing caramelization reaction
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Embodiment 1
[0030] A method for synthesizing high-purity sucrose monoester is carried out according to the following steps:
[0031] Step 1: Place sucrose, higher fatty acid ester, higher fatty acid salt, and catalyst in a high-energy ball mill for dry grinding, the ball milling speed is 400 r / min, the ball milling time is 5 hours, the protective atmosphere is nitrogen, and the ball milling is uniformly mixed to obtain a mixture, Wherein, the higher fatty acid ester is methyl stearate, the higher fatty acid salt is potassium stearate, the molar ratio of sucrose and higher fatty acid ester is 1:1, and the quality of higher fatty acid salt is sucrose and higher fatty acid ester 10% of the total mass, and the rest are catalysts. The catalyst is mixed with potassium carbonate and potassium hydroxide in a molar ratio of 1:2, and the molar ratio of potassium ions to sucrose in the catalyst is 2:5;
[0032] Step 2: Add the ball-milled mixture into a three-necked bottle, and preheat it in a vacuu...
Embodiment 2
[0039] The difference between this embodiment and the above-mentioned Embodiment 1 is that:
[0040] Step 3: The preheated mixture is placed in an induction furnace for heating and stirring, the protective atmosphere is nitrogen, the heating temperature is 110 ° C, and the stirring is performed for 5 hours, the stirring speed is 400 r / min, and the reaction pressure is 1.5 kPa to obtain a crude product;
[0041] Other conditions remain unchanged.
Embodiment 3
[0043] The difference between this embodiment and the above-mentioned Embodiment 1 is that:
[0044] Step 3: The preheated mixture is placed in an induction furnace for heating and stirring, the protective atmosphere is argon gas, the heating temperature is 100 ° C, and stirring is performed for 3 hours, the stirring speed is 400 r / min, and the reaction pressure is 1.5 kPa to obtain a crude product ;
[0045] Other conditions remain unchanged.
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