Ligne de traitement de contrôle automatique ISO de haute qualité

Erythritol Project Introduction

The dissolving tank receives the commercial starch, which is then added water to dissolve. After that, the starch milk enters a slurry mixing tank where its DS, PH value, and enzyme content are adjusted by online detection and control before moving on to an automatic liquefaction system. To achieve the finest liquefaction effect, use two-times ejection, two-times flashing, right temperature, and a specific time. Syrup is introduced to the saccharification system after liquefaction through PH adjustment and enzyme addition. When the DE or DX value required by the final product is obtained by adjusting the amount of enzyme and saccharification time, glucose enters the filtration stage to purge the product of any remaining protein and other contaminants. Following filtration, the liquid glucose is subjected to decolorization, filtering, and a continuous ion exchange system to remove colored impurities and impurity ions, enabling the glucose to fulfill its refining and purifying objectives. With the addition of strain and nutritive salt, the refined glucose enters the fermentation system and keeps the fermentation period constant. Prior beer entering the crystallizer for crystallization, the fermented mash is concentrated by the evaporator system. After centrifugal separation and drying, the desired erythritol product is obtained by maintaining the established cooling curve for the specified amount of time.