Industrielle effiziente automatische Dah -Herstellung von Geräten

DAH Project Introduction

Starch milk adjustment: The DS=28-32%, PH, and temperature of starch milk from the starch workshop are adjusted. Alternately, combine dry starch and water, then make adjustments to obtain the aforementioned conditions in the next section.

Liquefaction: With the help of a liquefaction enzyme and the jet cooker, starch milk is liquefied. To achieve the best liquefaction effect, two ejections are required. The material is subsequently transported to the following section after cooling in the flash tank following liquefaction.

Saccharification: The syrup is liquefied and then delivered to the saccharification tank. Enzymes are used to carry out the process. The required DE value is attained after a predetermined amount of reaction time. The glucose is subsequently sent to the subsequent step after cooling in the flash tank.

Filtration and decolorization: Enter the decolorization filtering system after taking the filter to filter out the protein and other contaminants from the glucose. Activated carbon must be used for decolorization at the proper temperature. The filter will eliminate the activated carbon after decolorization. The following stage 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.

Evaporation: To get the appropriate DS value, the glucose is concentrated after passing through the safety filter and being supplied into the evaporator system.

Crystallization: The qualifying glucose is supplied into the crystallizer system after sterilizing. Keep the time right, chill the crystals in accordance with the cooling curve, and then pass the glucose crystal to the separating section.

Separation: By using high speed centrifugation, the mother liquor is removed from the crystal. The decolorization section receives some of the mother liquor. A portion of the mother liquor is used to produce liquid glucose or is sold straight. The drying portion receives the qualified glucose crystals that have been separated and qualified.

Dissolving: Fill the dissolving tank with soft water. After heating, the DMH is poured to the dissolving tank and dissolved to produce the required DS value for the following stage.

Decolorization/filtration: The dextrose then goes through the decolorization filtration system after it has dissolved. Activated carbon must be used for decolorization at the proper temperature. The filter will eliminate the activated carbon after decolorization. The subsequent section receives the filtered dextrose.

Monohydrate dextrose cooking: To get the highest possible vacuum for the vacuum pan, start the vacuum pump first. In the vacuum pan, place the refined monohydrate dextrose for crystallization and evaporation. Obtain the anhydrous dextrose after maintaining for a predetermined period of time.

Separation: The mother liquid and crystallized anhydrous dextrose are separated in the centrifuge after the anhydrous dextrose has been buffered and crystallized by the crystallizer. The front monohydrate dextrose dissolving tank receives the divided mother liquor once more. The dryer system receives the crystal anhydrous dextrose and dries it.

Drying: Anhydrous dextrose with a moisture content of less than 1% is produced after crystal anhydrous dextrose has been dried using a fluidized bed drier method.