Method for treating crop straws by utilizing acidizing fermentation liquor backflow and applications thereof
A technology of crop straw and acidification fermentation, which is applied in fermentation, waste fuel, etc., can solve the problems of waste of straw resources, etc., and achieve the effects of increasing methane production, reducing digestion time, and improving the efficiency of digestion and gas production
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Embodiment 1
[0016] After the straw is mechanically crushed, it is air-dried. The 30-mesh powder was selected by sieving and mixed with the refluxing straw hydrolysis and acidification solution according to the solid-to-liquid ratio of 1:10 (mass ratio), and the pretreatment time was 24 hours. After pretreatment, the total chemical oxygen demand (TCOD) in the liquid phase of crop straw increased by 1453mg / L. After pretreatment, the straw enters the hydrolysis acidification tank through the sludge pump, and the hydraulic retention time is 48 hours. The measured straw concentration is 24.5%, and the pH value of the fermentation liquid drops to 3.46. After hydrolysis and acidification, the straw enters the methane production pool through the sludge pump, the hydraulic retention time is 150h, and the methane production increases by 67.4%.
Embodiment 2
[0018] After the straw is mechanically crushed, it is air-dried. The 40-mesh powder was selected by sieving and mixed with the refluxed straw hydrolysis and acidification solution according to the solid-to-liquid ratio of 1:16 (mass ratio), and the pretreatment time was 36 hours. After pretreatment, the total chemical oxygen demand (TCOD) in the liquid phase of crop straw increased by 2132mg / L. After pretreatment, the straw enters the hydrolysis acidification tank through the sludge pump, the hydraulic retention time is 24 hours, the measured straw concentration is 21.3%, and the pH value of the fermentation liquid drops to 3.03. After hydrolysis and acidification, the straw enters the methane production pool through the sludge pump, the hydraulic retention time is 190h, and the methane production is increased by 74.6%.
Embodiment 3
[0020] After the straw is mechanically crushed, it is air-dried. The 50-mesh powder was selected by sieving and mixed with the refluxed straw hydrolysis acidification solution according to the solid-to-liquid ratio of 1:18 (mass ratio), and the pretreatment time was 42 hours. After pretreatment, the total chemical oxygen demand (TCOD) in the liquid phase of crop straw increased by 2643mg / L. After the pretreatment, the straw enters the hydrolysis acidification tank through the sludge pump, the hydraulic retention time is 75h, the measured straw concentration is 32.7%, and the pH value of the fermentation liquid drops to 2.56. After hydrolysis and acidification, the straw enters the methane production tank through the sludge pump, the hydraulic retention time is 200h, and the methane production is increased by 83.4%.
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