Mixed raw-material fermenting process for producing alcohol
A technology of mixing raw materials and fermentation process, which is applied in the direction of fermentation and biofuel, etc., can solve the problem of reducing the amount of waste tank treatment, and achieve the effects of saving distillation steam consumption, reducing the amount of waste, and easy to handle
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example 1
[0018] Example 1: One-time addition method,
[0019] Take an alcohol plant with an annual output of 22,000 tons and take the cassava dry: sugarcane juice = 1:3 ingredient process as an example:
[0020] Use 18 tons of sugarcane juice per hour, add 6 tons of crushed cassava, in the mixing tank, adjust the slurry to the required concentration, 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 the high temperature resistant α-amylase and the slurry and stir evenly, and then use the pump to drive the slurry into the jet liquefier. The slurry and steam directly meet in the ejector. When the ejector processes the slurry, the effect of shearing and stirring is conducive to the uniform mixing and heating of the gas and liquid phases, and can ensure uniform heating and complete cooking of the particles in the slurry. The discharge temperature is controlled at 100~105℃; th...
Embodiment 2
[0029] Example 2: One-time addition method
[0030] Take an alcohol factory with an annual output of 18,000 tons, and take the ingredient process of dried sweet potato: sugarcane juice = 1:1 as an example:
[0031] Squeeze 6 tons of sugarcane juice and crush 6 tons of dried sweet potato per hour.
[0032] Mixing 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, stir the material liquid evenly, and pump the sugarcane juice powder slurry into the jet liquefier. The slurry and steam directly meet in the ejector. When the ejector processes the slurry, the effect of shearing and stirring is conducive to the uniform mixing and heating of the gas and liquid phases, and can ensure uniform heating and complete cooking of t...
example 3
[0040] Example 3: Two-time addition method
[0041] Take an alcohol plant with an annual output of 15,000 tons and take the ingredient process of dried cassava: sugarcane juice = 1:6 as an example:
[0042] Squeeze 18 tons of sugar cane juice per hour and crush 3.0 tons of dried cassava.
[0043] First mix with dried cassava: sugarcane juice=1:3, and mix with 9 tons (50%) sugarcane juice as the raw material of dried cassava powder. Adjust the slurry in the mixing tank. When the required concentration is reached, the 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, stir the material liquid evenly, and pump the sugarcane juice powder slurry into the jet liquefier. The slurry and steam directly meet in the ejector. When the ejector processes the slurry, the effect of shearing and stirring is conducive to the uniform mixi...
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