Erythritol Project Introduction
Starch milk adjustment: The DS=28-32%, PH, and temperature of starch milk from the starch workshop are adjusted. Alternately, combine the dried starch and water, then modify to meet the requirements in the next step.
Liquefaction: Using a jet cooker and a liquefaction enzyme, starch milk is liquefied. For the best liquefaction effect, ejection must occur twice. The material is transported to the following section after liquefaction and cooling in the flash tank.
saccharification: The saccharification tank receives the liquefied syrup. An enzyme is used to complete the process. The target DE value is attained following a specific amount of reaction time. After cooling in the flash tank, the glucose is subsequently delivered to the subsequent stage.
Filtration and decolorization: Enter the decolorization filtration system after taking the filter to filter the protein and other contaminants out of the glucose. Activated carbon at the proper temperature is necessary for decolorization. The filter will eliminate the activated carbon following decolorization. The subsequent section receives the filtered glucose.
Continuous ion exchange: To obtain pure and high-quality glucose, the glucose enters a continuous ion exchange system where the mixed impurity ions are removed using cation and anion resin.
Fermentation: Through the addition of produced seed and the necessary nutrients, at an appropriate temperature, and while maintaining a specific duration for the fermentation, qualified glucose enters the fermentation system.
Evaporation & crystallization: In order to get the right DS value for the crystallizer, the fermented mash is concentrated by the evaporator system. Erythritol crystals are produced via a specific time-dependent crystallization process.
Separation and drying: After crystallization, the erythritol crystals were separated using a centrifuge to produce the high-quality crystals and mother liquid. Qualified erythritol products were obtained after drying.