High yield method for combined production of crystallized fructose, mannitol and sorbierite
A technology for crystallizing fructose and mannitol, applied in the field of preparation of hexavalent alcohol, can solve the problems of difficult filtration, poor quality of mannitol and high production cost, and achieve the effects of reducing concentration consumption, reducing evaporation load and improving utilization rate
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Embodiment 1
[0040] (1) Starch raw material A is formulated into starch milk with a concentration of 30% by weight, and the pH is adjusted to 5.5 with soda ash. After adding high-temperature-resistant amylase, liquefaction and saccharification are carried out by conventional methods to obtain a concentration of 35% and a glucose value of 96. % invert sugar solution B.
[0041] (2) Invert sugar solution B is filtered, decolorized, and ion-exchange resin is used to remove impurities in a conventional manner, then evaporated to a dry matter weight percentage concentration of 50%, adjust the pH to 8.15, add 45ppm of magnesium ions, and dissolve at a temperature of 60°C. The isomerized sugar solution C containing 42% fructose, 53% glucose and 5% oligosaccharide was obtained after the reaction for 3 hours.
[0042] (3) Utilize the simulated moving bed device to process the isomerized sugar liquid C to separate fructose and glucose; use calcium-type cation exchange resin as the adsorbent, use wat...
Embodiment 2
[0053] (1) The starch raw material A is prepared into starch milk with a concentration of 27% by weight, the pH is adjusted to 5.8 with soda ash, and after adding high-temperature-resistant amylase, liquefaction and saccharification are carried out in a conventional method to obtain invert sugar solution B;
[0054] (2) Invert sugar solution B is filtered, decolorized, and ion-exchange resin is used to remove impurities in a conventional manner, then evaporated to a dry matter weight percentage concentration of 45%, adjust the pH to 8.25, add 43ppm of magnesium ions, and isotropic at a temperature of 58 ° C. After 2.5 hours of structuring reaction, isomerized sugar solution C containing fructose, glucose and oligosaccharides was obtained;
[0055] (3) Utilize the simulated moving bed device to process the isomerized sugar solution C to separate fructose and glucose; use calcium-type cation exchange resin as the adsorbent, and use water as the eluent to continuously feed, water,...
Embodiment 3
[0066] (1) The starch raw material A is prepared into starch milk with a concentration of 32% by weight, the pH is adjusted to 5.2 with soda ash, and after adding high-temperature-resistant amylase, liquefaction and saccharification are carried out in a conventional method to obtain invert sugar solution B;
[0067] (2) Invert sugar solution B is filtered, decolorized, and ion-exchange resin is used to remove impurities in a conventional manner, then evaporated to a dry matter weight percentage concentration of 55%, adjust the pH to 8.1, add 48ppm of magnesium ions, and isotropic at a temperature of 56°C. After 4 hours of structuring reaction, isomerized sugar solution C containing fructose, glucose and oligosaccharides was obtained;
[0068] (3) Utilize the simulated moving bed device to process the isomerized sugar solution C to separate fructose and glucose; use calcium-type cation exchange resin as the adsorbent, and use water as the eluent to continuously feed, water, and ...
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