1. Production capacity: *0 tons/day of *5% glucose syrup.
2. Product: *5% dry meter content of glucose syrup
3. Machine list
No |
Content |
Material |
|
1 |
*0tons/day glucose syrup production line equipment list |
|
|
2 |
Valve |
AISI**4+ABS |
|
3 |
Piping |
|
|
4 |
Electricity |
|
|
5 |
Instrument |
DCS automatic control |
|
6 |
Analytical apparatus |
Not including HPLC |
|
7 |
Spare parts |
Two year use |
|
4. Processing:
4.1Preparation for starch milk:
Refined starch from plant starch was dissolved into the water tank to be adjusted to *9~*0Be, then adding Na2CO3 to adjust the PH to 5.4~6.0, and adding α-amylase to be ready for liquefaction.
4.2. Liquefaction:
Put the starch milk prepared to the 1st injector and inject steam directly to the starch milk. Make the
temperature rise to **0ºC quickly. After entering the 1st flash evaporator, lower the temperature to *8ºC
and keep it for a certain time. The material, after initial hydrolysis, is with a lower viscidity.
The material is then put into the 2nd injector by the pump, its temperature reaching **5ºC quickly, then it
gets to the 2nd flash evaporator. The temperature in the 2nd flash evaporator declines to *5ºC. The DE
volume of the material would be between *5 and *0 after its staying in the tubular reactor for *****0
minutes.
4.3. Saccharification:
Put hydrochloric acid into the material after liquefaction and make the PH volume to 4.**4.5,
while
lowering the temperature from *0ºC to *0ºC. Add fungal enzymes and glucoamylase into it and keep
stirring at that temperature. DE value will be ≥*5 after the saccharification period will take *0 to *0hours.
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