Production method for crystalline tagatose
A production method and tagatose technology are applied in the production field of crystalline tagatose, can solve the problems of low lactose hydrolysis rate, low efficiency, unsuitable for industrial production and the like, and achieve the effect of high purity
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Embodiment 1
[0024] The best conditions for lactose enzymolysis: acid lactase is selected as lactase, the concentration of lactose is 40%, the dosage of enzyme is 0.02g per gram of lactose, the pH of the reaction is 5.2, the temperature is controlled at 50°C, and the result is measured after 4 hours of reaction , glucose 52.92%, galactose 43.93, residual lactose 3.07%.
Embodiment 2
[0026] Sequential simulated moving bed feed galactose: concentration 50%, of which galactose content is 43.32%, glucose content 52.62%, lactose content 4.06%, separation medium calcium resin, separation temperature is 60 ℃. The feed flow rate is 0.95L / h; the eluent flow rate is 1.50L / h; the separation product galactose flow rate is 1.15L / h; the separation by-product glucose flow rate is 1.3L / h; the circulation flow rate is 4.8L / h; the operating temperature is 60°C. The target purity value of the separated product is 90%; the valve opening time: 450-500 seconds. Separation results: in the galactose component, the concentration is 18.00%, of which the galactose content is 91.63%, the glucose content is 6.29%, and the lactose content is 1.08%; in the glucose component, the concentration is 20.50%, the galactose content is 5.85%, and the glucose content is 6.29%, The lactose content is 10.36%.
Embodiment 3
[0028] Select CaO as the isomerizing agent, the dosage is 0.375g CaO per gram of galactose, the concentration of galactose is 18.75%, the reaction temperature is 20°C, the reaction time is 2 hours, and the pH is adjusted to 5.8 with phosphoric acid for neutralization to obtain tagatose The highest content can reach 74.58%.
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