Method for improving excess activated sludge anaerobic fermentation hydrogen production efficiency
A technology of sludge anaerobic fermentation and residual activity, applied in the field of resource utilization of organic waste, can solve problems such as insignificant effect, achieve the effect of improving the degree of resource utilization, improving the hydrogen production capacity of fermentation, and improving efficiency
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Embodiment 1
[0013] (1) Concentrate the remaining activated sludge from the sewage treatment plant. The total suspended solids (TSS) of the concentrated sludge is 10.6g / L, and the volatile suspended solids (VSS) is 6.9g / L. No other pretreatment process is required.
[0014] (2) Divide the concentrated sludge into two 500mL reactors, each reactor is equipped with 400mL concentrated sludge, adjust the initial pH of the sludge in the reactor to 10.06-10.14, and blow off the exhaust gas After the oxygen environment, one reactor was fermented in a shaking table at 37°C, and the other was fermented in a shaking table at 55°C. The fermentation process lasted for 6 days. The control is 10 for alkaline conditions. The content of gas components is determined by a gas chromatograph, and the gas volume is collected by a gas collection bag. After the reactor runs stably, the hydrogen output in the two reactors is as shown in Table 1:
[0015] Table 1 Effect of temperature on alkaline fermentation hyd...
Embodiment 2
[0019] (1) Concentrate the remaining activated sludge from the sewage treatment plant. The total suspended solids (TSS) of the concentrated sludge is 10.6g / L, and the volatile suspended solids (VSS) is 6.9g / L. No other pretreatment process is required.
[0020] (2) Divide the concentrated sludge into three 500mL reactors, each reactor is equipped with 400mL concentrated sludge, adjust the initial pH of the sludge in the reactor to 8, 9, 10, and use nitrogen to Air stripping creates an anaerobic environment, and the reactors are placed in a shaking table at 55°C for anaerobic fermentation, and the hydraulic retention time is 6 days. During the fermentation process, 4M NaOH was added dropwise through the pH automatic titrator to always control the sludge in the three reactors to be 8, 9, and 10 respectively. During the operation of the reactor, the gas component content is measured by a gas chromatograph, and the gas volume is collected by a gas collection bag. After the reacto...
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