Mixed raw-material fermenting process for producing alcohol
A technology of mixing raw materials and fermentation process, applied in the direction of fermentation, biofuel, etc., can solve the problem of reducing waste tank processing capacity, etc., and achieve the effect of saving the consumption of distillation steam, reducing the concentration of solids, and reducing the amount of waste discharged.
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example 1
[0018] Example 1: one-time addition method,
[0019] Taking an alcohol factory with an annual output of 22,000 tons, taking cassava: sugarcane juice = 1:3 batching process as an example:
[0020] Use 18 tons of sugarcane juice per hour, add 6 tons of crushed cassava, adjust the slurry to the required concentration in the mixing tank, control the temperature of the slurry at 60-65°C, and add an appropriate amount of amylase. In the liquefaction tank, adjust the pH value to 5.2-5.5, and add Ca 2+ , add high-temperature resistant α-amylase and slurry, stir evenly, and then pump the slurry into the jet liquefier. In the injector, the slurry and the steam meet directly. When the injector processes the slurry, the effect of shearing and stirring is conducive to the uniform mixing and heating of the gas-liquid two phases, which can ensure the uniform heating and complete cooking of the particles in the slurry. Control the discharge temperature at 100-105°C; the feed liquid coming o...
Embodiment 2
[0029] Embodiment 2: one-time addition method
[0030] Taking an alcohol factory with an annual output of 18,000 tons, taking the ingredient process of dried sweet potato: sugarcane juice = 1:1 as an example:
[0031] Squeeze 6 tons of sugar cane juice per hour, and crush 6 tons of dried sweet potatoes.
[0032] Mix with dried sweet potato: sugarcane juice = 1:1, adjust the slurry to the required concentration in the mixing tank, control the temperature of the slurry at 60-65°C, and add an appropriate amount of amylase. In the liquefaction tank, adjust the pH value to 5.2-5.5, and add Ca 2+ , add high-temperature-resistant α-amylase, feed liquid and stir evenly, and pump the sugarcane juice powder into the jet liquefier. In the injector, the slurry and the steam meet directly. When the injector processes the slurry, the effect of shearing and stirring is conducive to the uniform mixing and heating of the gas-liquid two phases, which can ensure the uniform heating and complet...
example 3
[0040] Example 3: Secondary addition method
[0041] Taking an alcohol factory with an annual output of 15,000 tons, taking cassava: sugarcane juice = 1:6 batching process as an example:
[0042] Squeeze 18 tons of sugar cane juice per hour, crush 3.0 tons of dried cassava.
[0043] Carry out mixing with dried cassava: about 1:3 of sugarcane juice=1: 3 earlier, carry out mixing with 9 tons (promptly using 50%) sugarcane juice as the mixing water of cassava dry powder raw material first, in mixing tank, adjust slurry When the desired concentration is reached, the product temperature of the slurry is controlled at 60-65°C, and an appropriate amount of amylase is added. In the liquefaction tank, adjust the pH value to 5.2-5.5, and add Ca 2+ , add high-temperature-resistant α-amylase, feed liquid and stir evenly, and pump the sugarcane juice powder into the jet liquefier. In the injector, the slurry and the steam meet directly. When the injector processes the slurry, the effect...
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