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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Embodiment 1
[0018] Two sets of membrane-bioreactors treat the same urban domestic sewage, the designed hydraulic retention time is 8 hours, and the sludge age is 90 days. The membrane components are made of polyvinylidene fluoride (PVDF) flat membranes, the membrane pore size is 0.20 μm, and the membrane flux is constant at 25L / (h·m 2 ); wherein the experimental group added fillers, the fillers were honeycomb plastic fillers, and the amount of fillers added was 5% of the reactor volume, and the other group was used as a control group. The operation results show that the membrane cleaning cycle of the experimental group is 120d, and the energy consumption is 0.51kwh / m 3 , the membrane cleaning period of the blank group is 50d, and the energy consumption is 0.55kwh / m 3 .
Embodiment 2
[0020] Two sets of membrane-bioreactors treat the same industrial wastewater, the design hydraulic retention time is 10h, the sludge age is 120d, the membrane module is made of flat polyvinyl chloride (PVC) membrane, the membrane pore size is 0.25μm, and the membrane flux is constant at 15L / (h·m 2 ); wherein the experimental group added fillers, the fillers were corrugated plate hard polyvinyl chloride fillers, and the amount of fillers added was 10% of the reactor volume, and the other group was used 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 period of the blank group is 35d, and the energy consumption is 0.59kwh / m 3 .
Embodiment 3
[0022] Two sets of membrane-bioreactors treat the same fecal sewage, the design hydraulic retention time is 8h, the sludge age is 90d, the membrane module is made of polyvinylidene fluoride (PVDF) flat membrane, the membrane pore size is 0.20μm, and the membrane flux is constant at 20L / (h·m 2 ); wherein the experimental group added fillers, the fillers were soft fibrous fillers, and the amount of fillers added was 5% of the reactor volume, and the other group was used as a control group. The operation results show that the membrane cleaning cycle of the experimental group is 100d, and the energy consumption is 0.51kwh / m 3 , the membrane cleaning period of the blank group is 45d, and the energy consumption is 0.56kwh / m 3 .
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