A method of using redox mediator to promote the fermentation of excess sludge to produce acid
A technology of excess sludge and mediator, which is applied in the field of sludge treatment and disposal in sewage treatment plants in environmental protection, to achieve the effects of increasing activity, increasing the amount of acid produced by fermentation, and accelerating the rate of acid production
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Embodiment 1
[0019] The redox mediator used is AQDS, and adding AQDS to the NaOH solution with a pH of 10 is prepared into an AQDS stock solution with an AQDS concentration of 1.0 g / L; the remaining sludge comes from a city sewage treatment plant in Hangzhou, Zhejiang Province The sludge (after dehydration) has a TSS content of 138 g / L.
[0020] Add 217 mL of excess sludge to both fermenter R0 (effective volume 3.0 L) and fermenter R1 (effective volume 3.0 L), and then make up 3.0 L with distilled water. At this time, the remaining sludge TSS in the fermenter is 10 g / L; the remaining sludge in the fermenter was first stirred at 30 rpm for 1 h, and then 1.5 mL of AQDS stock solution was quickly added to fermenter R1, and the concentration of AQDS in the fermentation system was 0.5 mg / L. Fermenter R0 was used as a control group without adding AQDS stock solution. In the fermentation tank R0 and the fermentation tank R1, the fermentation temperature is controlled at 15°C, the pH value of th...
Embodiment 2
[0023] The redox mediator used is AQS, and adding AQS in the KOH solution that pH is 12 is mixed with the AQS stock solution that AQDS concentration is 5.0g / L; The sludge (after dehydration) has a TSS content of 138 g / L.
[0024] Add 870 mL of excess sludge to both fermenter R0 (effective volume 3.0 L) and fermenter R1 (effective volume 3.0 L), and then make up 3.0 L with distilled water. At this time, the TSS in the fermenter is 40 g / L; The remaining sludge in the fermenter was first stirred at 60 rpm for 6 h, and then 12 mL of AQS stock solution was quickly added to the fermenter R1. At this time, the concentration of AQDS in the fermentation system was 20 mg / L. Fermenter R0 was used as a control group without adding AQS stock solution. In the fermentation tank R0 and fermentation tank R1, the fermentation temperature is controlled at 35°C, the pH value of the fermentation system is adjusted to 9.0 with KOH solution, and the oxidation-reduction potential is controlled at -1...
Embodiment 3
[0027] The redox mediator used was menaquinone, Ca(OH) at pH 10 2 The solution was prepared into a 50 g / L mechanone stock solution; the excess sludge was derived from the biochemical treatment process excess sludge of a starch factory sewage treatment station in Hangzhou, and the TSS content was 65 g / L.
[0028] Add 1385 mL of excess sludge to both fermenter R0 (effective volume 3.0 L) and fermenter R1 (effective volume 3.0 L), and then make up 3.0 L with distilled water. At this time, the TSS in the fermenter is 70 g / L; The remaining sludge in the fermenter was first stirred at 100 rpm for 2 h, and then 15 mL of methionine stock solution was quickly added to R1. At this time, the concentration of methionone in the fermentation system was 100 mg / L. Fermentation tank R0 was used as a control group without adding methaquinone stock solution. In fermentor R0 and fermenter R1, the fermentation temperature is controlled at 25°C, the pH of the fermentation system is maintained at 8...
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