A New Method to Control Membrane Fouling in Membrane-Bioreactor
A bioreactor, biofilm technology, applied in chemical instruments and methods, biological water/sewage treatment, sustainable biological treatment, etc. Energy consumption, mitigation of membrane fouling, effect of optimizing membrane fouling situation
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Example Embodiment
[0017] [Example 1]
[0018] Two sets of membrane-bioreactors treat the same urban domestic sewage, with a designed hydraulic retention time of 8h and a sludge age of 90d. The membrane module uses PVDF flat membranes with a membrane pore size of 0.20μm and a constant membrane flux of 25L / (h·m 2 ); Among them, the experimental group was fed with fillers, the fillers were honeycomb plastic fillers, and the filler dosage was 5% of the reactor volume, and the other group served as a control group. The operation results show that the membrane cleaning cycle of the experimental group is 120 days, and the energy consumption is 0.51kwh / m 3 , The membrane cleaning cycle of the blank group is 50d, and the energy consumption is 0.55kwh / m 3 .
Example Embodiment
[0019] [Example 2]
[0020] Two sets of membrane-bioreactors treat the same industrial wastewater. The designed hydraulic retention time is 10h and the sludge age is 120d. The membrane module uses a polyvinyl chloride (PVC) flat membrane with a membrane pore size of 0.25μm and a constant membrane flux of 15L / (h·m 2 ); Among them, the experimental group was filled with fillers, which were corrugated plate hard polyvinyl chloride fillers, and the filler dosage was 10% of the reactor volume, and the other group served as a control group. The operation results show that the membrane cleaning cycle of the experimental group is 87 days and the energy consumption is 0.53kwh / m 3 , The membrane cleaning cycle of the blank group is 35d, and the energy consumption is 0.59kwh / m 3 .
Example Embodiment
[0021] [Example 3]
[0022] Two sets of membrane-bioreactors treat the same fecal sewage. The designed hydraulic retention time is 8h and the sludge age is 90d. The membrane module adopts a polyvinylidene fluoride (PVDF) flat membrane with a membrane pore size of 0.20μm and a constant membrane flux of 20L / (h·m 2 ); Among them, the experimental group was fed with fillers, the fillers were soft fibrous fillers, the filler dosage was 5% of the reactor volume, and the other group served as a control group. The operation results show that the membrane cleaning cycle of the experimental group is 100 days, and the energy consumption is 0.51kwh / m 3 , The membrane cleaning cycle of the blank group is 45d, and the energy consumption is 0.56kwh / m 3 .
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