Высококачественный автоматический управление производством мальтита

Maltitol Project Introduction

Starch milk adjustment: Starch milk must be adjusted to the proper PH, DS, and temperature. The correct value for the adjusted DS is DS=28%-32%. Dry starch is another option. To achieve the appropriate DS level, add the water mixed with dried starch. The starch milk is then delivered to the following area for liquefaction and additional processing after being given the aforementioned condition.

Liquefaction: Liquefied syrup is made by the process of liquefaction. Milk that has been starched is transferred to the liquefaction system, where an enzyme is added to create the liquefaction effect. The liquefaction improves after two ejections. The material is transferred to the flash tank for cooling after liquefaction before moving on to the next step.

Saccharification: To get the necessary DE value, saccharification is used. The syrup is liquefied and then delivered to the saccharification tank. An enzyme helps the process to occur. It reacts for a certain amount of time before reaching the target DE value. After that, the maltose is transferred to the flash tank to cool. The maltose is then sent on to the following phase.

Filtration and decolorization: Protein and other contaminants are eliminated through filtration. Activated carbon is used in decolorization to remove the colored ion. The filter also gets rid of the activated carbon. The maltose is transferred to the following section after filtration and decolorization.

Continuous ion exchange: The mixed ion contaminants are removed by continuous ion exchange systems. Resin is placed inside the ion exchange device. On the basis of their chemical principles, cation and anion resin eliminates mixed ion contaminants. The maltose then attains a high degree of purity.

Hydrogenation reaction: Maltose is converted into maltitol through the process of hydrogenation. For hydrogenation reactions, hydrogen is used. The maltose undergoes reaction to become crude maltitol, which is then transferred to a flash tank for cooling. A sedimentation tank was used for the raw maltitol.

Precipitation and filtration: The nickel catalyst that is still present in the maltitol is filtered out and reused in the front portion. The raw maltitol undergoes filtration after precipitation. The refined part receives the crude maltitol that has been filtered.

Decolorization/filtration: Utilizing activated carbon, decolorization removes colored ions and pigment. The filter then removes the activated carbon. The following step receives the filtered maltitol for additional processing.

Continuous ion exchange: To achieve a high purity level, the combined impurity ions in the maltitol must be removed. The mixed impurity ions are removed from the maltitol by the continuous ion exchange system. Cation and anion resin is used to fill the ion exchange system. Purity and excellent quality are attained by the maltitol after a continuous ion exchange method.

Evaporation: Maltitol is concentrated using an evaporator to achieve the appropriate DS value. The safety filter is used to filter the refined maltitol before it is delivered into the evaporator system for concentration to achieve the appropriate DS value. Finally, the high-quality maltitol product is acquired.