Sorbitol Project Introduction
Commercial starch added and combined with water is used to dissolve it in the tank. The starch milk is online recognized and regulated in the slurry mixing tank to correct for DS, PH value, and enzyme amount before entering the automatic liquefaction system. To achieve the optimum liquefaction outcome, use twice as much ejection and flashing, maintain the proper temperature, wait a particular amount of time, and use twice as much heat. The syrup is liquefied and then delivered to the saccharification device after the PH is adjusted and enzymes are added. The syrup enters the filtration process to eliminate the less protein and other contaminants incorporated in the product after attaining the DE or DX value required by the end product by altering the amount of enzyme and saccharification. The liquid syrup goes through decolorization, filtering, and a continuous ion exchange system to eliminate colored impurities and impurity ions, which helps the syrup achieve its purification and refining goals. After being concentrated by the evaporator, it enters the high-pressure hydrogenation reactor for the hydrogenation reaction. After the reaction, the nickel catalyst added to the sorbitol solution is filtered and used once more. For the sorbitol solution to achieve its refining and purifying goals, impurities and ions must be removed via decolorization, filtering, and a continuous ion exchange system. The right amount of sorbitol was produced after concentration using an evaporator.