The whole system includes:
Liquefaction---Saccharifying---Filtering---Decoloring---Ion exchange---Evaporation and concentration---Crystallization---Separation and drying ---Maltodextrin Production ---Washing In Place
Glucose Maltose and Maltodextrin Production Line
Brief Indtroduction:
Use different kinds of refined starch, such as corn starch, wheat starch or cassava as raw material to produce malt dextrin or glucose by the methods of acid hydrolysis or enzyme hydrolysis.
Acid hydrolysis is easily to produce some colorful material or non-fermentable sugar, because of adverse effect, in practice this method is stopped. We provide plants with enzyme hydrolysis to produce glucose or malt dextrin.
Theoretically, when DE value is less than 20%, i.e., reducing sugar contents is less than 20%, it is called as malt dextrin. But in daily use, the separation is not very clear.
Customers that are interested, please contact us for further details. We can supply budget of the total investment, area occupied, utilies consumption based on each ton, and other relative information for customers to make decision.
| Specification | LPG-5 | LPG-25 | LPG-50 | LPG-100 | LPG-150 | LPG-200 |
| Air Inlet temperature | 140-550 ° C (depend on the product to be dried, and URS) | |||||
| Air exhaust temperature | 60-120 ° C (depend on the product to be dried, and URS) | |||||
| Nominal water evaporationcapacity (Kg / h) | 5 | 25 | 50 | 100 | 150 | 200 |
| Heating method | High-pressure steam, or steam + electricity, or any kinds of fuel (diesel, natural gas, liquefiedpetroleum gas or coal, etc.), or solid fuel (any combustible material). Please specify. | |||||
| Drying tower diameter (mm) | 1100 | 1800 | 2150 | 2560 | 2860 | 3200 |
| Overall Dimensions (m) | 2×1.4×2.2 | 5×3×4 | 6×4×5 | 8×4×6 | 8×5×7 | 10×5×8 |
| Product yield | 95-99.9%_depend on the properties of the product and configurations |
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