| 利用边界层理论确定预涂动态膜生物反应器稳定曝气量的试验研究 |
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| 中文关键词 预涂动态膜 边界层 曝气量 平板膜 |
| 英文关键词 precoated dynamic membrane boundary layer aeration intensity flat membrane |
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| 中文摘要 |
| 研究了膜生物反应器中低浓度活性污泥的流变性,确定当污泥浓度低于8000mg?L-1时的泥水混合液近似于牛顿流体,进而利用牛顿流体力学中边界层理论计算预涂动态膜(PDM)厚度等于平板膜表面层流边界层厚度时的稳定曝气量.为保证预涂动态膜生物反应器(PDMBR)运行的稳定性,在其运行初期选择满足生物所需最佳溶解氧(DO)3～5mg?L-1的供氧曝气量,随后逐渐增加到稳定曝气量的运行方式.实验结果表明,此运行方式能较好地提高动态膜的稳定性,在稳定运行的31d内出水COD低于12.48 mg?L-1,平均去除率达到97.49%,NH4+-N约为5.27 mg?L-1,平均去除率为76.13%,而操作压力仅上升至27kPa.试验后期考察了PDMBR在高于稳定曝气量下运行的稳定性,发现PDM发生脱落,从而证明利用边界层理论确定的预涂类动态膜的稳定曝气量具有一定的应用价值. |
| 英文摘要 |
| The rheological behaviour of the low sludge concentration liquor in MBR was investigated and made a conclusion that this liquor approximated to the Newtonian fluid while the concentration of the sludge was less than 8000 mg?L-1. Furthermore, when the laminar flow boundary layer thickness on the surface of flat membrane came up to the thickness of precoated dynamic membrane (PDM), the steady aeration intensity was calculated by using the boundary layer theory in the Newtonian hydrodynamics. In order to ensure the stability of the pre-coated dynamic membrane bioreactor (PDMBR), oxygen supply aeration intensity was chosen to supply the best dissolved oxygen (3～5 mg?L-1) in the initial stages and gradually increased to the steady aeration intensity. The results indicated that this mode could enhance the stability of PDM. In the experiment period (31d), effluent COD was less than 12.48 mg?L-1 and its average removal rate was 97.49%, NH4+-N was less than 5.27 mg?L-1 and its average removal rate was 76.13%, while the operational pressure just increased to 27 kPa. During the last period of the experiment, the stability of the PDMBR was studied when the aeration intensity was more than the steady aeration intensity and it was found that the precoated layer had been brushed off from the surface of common filter cloth, so this phenomenon proved that using the boundary layer theory could determine steady aeration intensity of PDMBR. |
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