A process for simultaneous production of lactulose and tagatose
A lactulose and process technology, applied in the field of simultaneous production of lactulose and tagatose, can solve the problems of low purity of lactulose, difficulty in crystallization, and insufficient utilization of lactulose, so as to achieve full utilization of resources, good separation effect, and efficient operation low cost effect
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Embodiment 1
[0030] Example 1: Weigh 50kg of lactose, add deionized water to make the lactose aqueous solution mass concentration 40%, then add 2.5kg of anhydrous sodium salt, heat to 110°C after reflux with condensed water, and maintain 110°C for isomerization for 3 hours, then cool , activated carbon decolorization, ion exchange, evaporation and concentration to carry out lactose crystallization, centrifuged to obtain lactulose syrup with a lactose content of 8.86%, a lactulose content of 70.15%, and a galactose content of 20.04%; the mass concentration of the obtained lactulose syrup was adjusted to 50% , enter the ternary sequential simulated moving bed at a speed of 3.0L / h, and separate at 60°C with a switching time of 17 minutes, the purity of the lactulose component is 91.17%, and the purity of the galactose component is 70.32%; Concentrate the purified lactulose component to 85%, add lactulose seed crystals at 2.0%, and then cool, the cooling rate is 0.3°C / h at 60-50°C, 0.5°C / h at 5...
Embodiment 2
[0031]Example 2: Weigh 50kg of lactose, add deionized water to make the lactose aqueous solution mass concentration 60%, then add 5kg of anhydrous sodium salt, heat to 120°C after refluxing condensed water, and maintain 120°C for isomerization for 1 hour, cool, Activated carbon decolorization, ion exchange, evaporation and concentration are followed by lactose crystallization. After centrifugation, a lactulose syrup with a lactose content of 9.23%, a lactulose content of 68.21%, and a galactose content of 21.82% is obtained; the mass concentration of the obtained lactulose syrup is adjusted to 60%. Enter the three-way sequential simulated moving bed at a speed of 2.0L / h, and separate at 50°C and a switching time of 21 minutes to obtain a lactulose component with a purity of 89.88% and a galactose component with a purity of 75.43%; The purified lactulose component was concentrated to 90%, added lactulose seed crystals at 1.0%, cooled the syrup from 60°C to 15°C at a speed of 0.5...
Embodiment 3
[0032] Example 3: Weigh 50kg of lactose, add deionized water to make the mass concentration of lactose aqueous solution 20%, then add 0.5kg of anhydrous sodium salt, heat to 90°C after reflux with condensed water, and maintain 90°C for isomerization for 6h, cool , activated carbon decolorization, ion exchange, evaporation and concentration to carry out lactose crystallization, after centrifugation to obtain lactulose syrup with a lactose content of 9.37%, a lactulose content of 66.57%, and a galactose content of 23.05%; the mass concentration of the obtained lactulose syrup was adjusted to 40% , enter the three-way sequential simulated moving bed at a speed of 4.0L / h, and separate at 50°C with a switching time of 13 minutes. The purity of the lactulose component is 90.08%, and the purity of the galactose component is 78.53%; Concentrate the purified lactulose component to 75%, add lactulose seed crystals at 5.0%, and then cool, the cooling rate is 0.8°C / h at 60-50°C, 0.5°C / h at...
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