Combined pretreatment method for enhancing excess sludge anaerobic fermentation to produce short-chain volatile fatty acid
A volatile fatty acid, anaerobic fermentation technology, applied in the field of ultrasonic and free ammonia joint pretreatment of excess sludge to produce short-chain volatile fatty acids, can solve the problem of weak inhibition, limited ability to degrade organic matter, unfavorable short-chain volatile fatty acids Accumulation and other issues, to achieve the effect of resource utilization and recycling
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Embodiment 1
[0026] First, the residual sludge in the secondary sedimentation tank of the sewage treatment plant is concentrated, and the sludge is used as the fermentation substrate. The processing steps are as follows:
[0027] Step 1: Ultrasonic pretreatment, the ultrasonic sound energy density is 2w / ml, and the ultrasonic time is 15min;
[0028] Step 2: Free ammonia pretreatment, add a certain amount of 4mol / L ammonium chloride solution to the sludge, so that the initial ammonia nitrogen concentration in the remaining sludge is 113.7mg / L, use 4mol / L NaOH solution and 4mol / L 1 L of HCl solution adjusted the pH of the remaining sludge to 9, and maintained it for 48 hours, during which the temperature was controlled at 25 ± 0.1 °C (under this condition, the initial free ammonia concentration was 50 mg NH 3 -N / L), the sludge mechanical stirring speed is 120rpm / min.
[0029] Step 3: On the third day of fermentation, the reactor is filled with nitrogen to drive oxygen, and the temperature ...
Embodiment 2
[0032] First, the residual sludge in the secondary sedimentation tank of the sewage treatment plant is concentrated, and the sludge is used as the fermentation substrate. The processing steps are as follows:
[0033] Step 1: Ultrasonic pretreatment, the ultrasonic sound energy density is 2w / ml, and the ultrasonic time is 15min;
[0034] Step 2: Free ammonia pretreatment, add a certain amount of 4mol / L ammonium chloride solution to the sludge, so that the initial ammonia nitrogen concentration in the remaining sludge is 227.4mg / L, use 4mol / L NaOH solution and 4mol / L 1 L of HCl solution adjusted the pH of the remaining sludge to 9, and maintained it for 48 hours, during which the temperature was controlled at 25 ± 0.1 ° C (under this condition, the initial free ammonia concentration was 100 mg NH 3 -N / L), the sludge mechanical stirring speed is 120rpm / min.
[0035] Step 3: On the third day of fermentation, the reactor is filled with nitrogen to drive oxygen, and the temperatur...
Embodiment 3
[0038] First, the residual sludge in the secondary sedimentation tank of the sewage treatment plant is concentrated, and the sludge is used as the fermentation substrate. The processing steps are as follows:
[0039] Step 1: Ultrasonic pretreatment, the ultrasonic sound energy density is 2w / ml, and the ultrasonic time is 15min;
[0040] Step 2: Free ammonia pretreatment, add a certain amount of 4mol / L ammonium chloride solution to the sludge, so that the initial ammonia nitrogen concentration in the remaining sludge is 341mg / L, use 4mol / L NaOH solution and 4mol / L HCl solution to adjust the pH of the remaining sludge to 9, and maintain it for 48h, during which the temperature is controlled at 25±0.1°C (under this condition, the initial free ammonia concentration is 150mg NH 3 -N / L), the sludge mechanical stirring speed is 120rpm / min.
[0041] Step 3: On the third day of fermentation, the reactor is filled with nitrogen to drive oxygen, and the temperature is controlled at 25±...
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