Method for preparing fermentation carbon source by hydrolysis and acidification of biomass raw materials
A biomass raw material, hydrolysis and acidification technology, applied in the direction of fermentation, etc., can solve the problems of low hydrolysis efficiency of lignocellulose, increase the production cost of products, etc., and achieve the effect of saving consumption, increasing concentration, and cheap fermentation carbon source
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Embodiment 1
[0026] 1) The corn stalks are pretreated by steam explosion, dried and crushed to 20 mesh;
[0027] 2) Using the domesticated activated sludge as the seed sludge, mix the steam explosion pretreated corn stalks evenly with the mass ratio of 1:1 to the activated sludge, then add water to adjust the solid-liquid ratio to 1:10, and adjust the pH to After 5.5, nitrogen gas was introduced into the reaction system, and anaerobic acidification was carried out at 35°C for 5 days.
[0028] 3) Solid-liquid separation is carried out after acidification, and the acidified liquid obtained by acidification is used as a fermentation carbon source of PHA.
Embodiment 2
[0030] 1) The corn stalks are pretreated with dilute acid, dried and crushed to 40 mesh;
[0031] 2) Using the domesticated activated sludge as the seed sludge, mix the dilute acid pretreated corn stalks evenly with the mass ratio of 1:1 to the activated sludge, then add water to adjust the solid-liquid ratio to 1:5, and adjust the pH to After 6.0, nitrogen gas was introduced into the reaction system, and anaerobic acidification was carried out at 37°C for 4 days.
[0032] 3) Solid-liquid separation is carried out after acidification, and the acidified liquid obtained by acidification is used as a fermentation carbon source of PHA.
Embodiment 3
[0034] 1) After the wheat straw is pretreated by steam explosion, it is dried and crushed to 20 mesh;
[0035] 2) Using the domesticated activated sludge as the seed sludge, mix the steam explosion pretreated wheat straw with the activated sludge mass ratio of 5:1 evenly, then add water to adjust the solid-liquid ratio to 1:8, and adjust the pH to After 6.0, nitrogen gas was introduced into the reaction system, and anaerobic acidification was carried out at 37°C for 5 days.
[0036] 3) Solid-liquid separation is carried out after acidification, and the acidification solution is used as a fermentation carbon source for cutinase.
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