Treatment method for efficient anaerobic production of acid and gas from kitchen waste
A technology of kitchen waste and a treatment method is applied in the field of efficient anaerobic acid production and gas production of kitchen waste, so as to achieve the effects of speeding up the process of biogas production, avoiding excessive organic content and high biogas production efficiency
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Embodiment 1
[0030] Embodiment one (sequential batch type):
[0031] The pretreated kitchen waste and anaerobic residual sludge were mixed in a mass ratio of 5:1, the solid content of the mixture was 5%, and the concentration of volatile fatty acids (VFA) in the mixed solution before fermentation was 1.5mmol / L. The pH is 5.8, the operating conditions of the acid production equipment are set at a temperature of 35.0°C, a stirring speed of 90 rpm, and the acid production fermentation tank is operated for 5 days, the pH reaches 3.75, and the concentration of VFA in the mixed solution after fermentation is 88.5mmol / L.
[0032] After the acid-producing fermentation is completed, the mixed liquid is pumped into the solid-liquid separation device. After separation, 20% of the separated liquid is pumped into the gas-producing reactor, where it is mixed with the anaerobic sludge mixed liquid at a ratio of 1:10 , the operating conditions of the gas production equipment were set at a temperature of 3...
Embodiment 2
[0033] Embodiment two (sequential batch formula):
[0034]The pretreated kitchen waste and anaerobic residual sludge were mixed at a mass ratio of 4:1, the solid content of the mixture was 10%, the VFA concentration in the mixed solution before fermentation was 3.45 mmol / L, and the pH was 5.3. The operating conditions of the acid equipment are set at a temperature of 35.0°C, a stirring speed of 90 rpm, and the acid-producing fermentation tank is operated for 5 days, the pH reaches 3.1, and the concentration of VFA in the mixed liquid after fermentation is 108.8mmol / L.
[0035] After the acid-producing fermentation is completed, the mixed liquid is pumped into the solid-liquid separation device. After separation, 20% of the separated liquid is pumped into the gas-producing reactor, where it is mixed with the anaerobic sludge mixed liquid at a ratio of 1:8 , the operating conditions of the gas production equipment were set at a temperature of 35.0°C and a stirring speed of 90rpm...
Embodiment 3
[0036] Embodiment three (continuous)
[0037] The pretreated kitchen waste and anaerobic residual sludge were mixed at a mass ratio of 5:1, the solid content of the mixture was 5%, the VFA concentration in the mixed solution before fermentation was 1.5mmol / L, and the pH was 5.8. The operating conditions of the acid equipment were set at a temperature of 35.0°C and a stirring speed of 90 rpm. The acid-producing fermenter was run for 5 days, the pH reached 3.75, and the concentration of VFA in the mixed liquor after fermentation was 88.5mmol / L. Turn on the peristaltic pump and pump it into the solid-liquid separation device at a flow rate of 10ml per minute. The solid-liquid separation device will separate the mixed liquid at a flow rate of 10ml per minute to the gas generating reactor, and the acid generating reactor will feed 10ml of food waste and anaerobic residue per minute. Sludge is mixed with liquid at a mass ratio of 5:1. The hydraulic retention time is 5 days, and the...
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