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[使用微气泡曝气生物膜反应器处理废水]

[Wastewater treatment using a microbubble aerated biofilm reactor].

作者信息

Zhang Lei, Liu Ping, Ma Jin, Zhang Jing, Zhang Ming, Wu Gen

机构信息

School of Environmental Science and Engineering, Hebei University of Science and Technology, Shijiazhuang 050018, China.

出版信息

Huan Jing Ke Xue. 2013 Jun;34(6):2277-82.

Abstract

Microbubble aeration is supposed to be able to provide potential advantage for aerobic biological wastewater treatment due to enhancement of oxygen mass transfer. Biofilm reactor is considered to be feasible for application of microbubble aeration. Shirasu porous glass (SPG) membrane was used for microbubble aeration in a biofilm reactor to treat synthetic municipal wastewater. The air permeability of SPG membranes, dissolved oxygen (DO) concentration, pollutant removal and oxygen utilization were investigated during the continuous operation of the bioreactor. The long-term stable continuous operation of the experimental system demonstrated the successful application of microbubble aeration in aerobic wastewater treatment processes. The air permeability of SPG membranes was influenced by its surface wettability and pore size. The air permeability of hydrophobic membrane was better than that of hydrophilic membrane. The air permeability could also be improved by increasing the pore size. DO concentration was affected by organic loading mainly at a certain air flux. The optimal SPG membrane area-based COD removal capacity of the experimental system was determined as 6.88 kg x (m2 x d)(-1). NH4(+)-N removal was mainly affected by DO concentration and its diffusion inside the biofilm. The simultaneous nitrification and denitrification was observed at a high organic loading rate. The oxygen utilization was much more efficient in microbubble aeration, compared to traditional bubble aeration, and it might be close to 100% at optimal running conditions.

摘要

由于强化了氧的传质,微气泡曝气被认为能够为好氧生物废水处理提供潜在优势。生物膜反应器被认为适用于微气泡曝气。采用白榴石多孔玻璃(SPG)膜在生物膜反应器中进行微气泡曝气以处理模拟城市污水。在生物反应器连续运行期间,研究了SPG膜的透气率、溶解氧(DO)浓度、污染物去除情况及氧利用率。实验系统的长期稳定连续运行证明了微气泡曝气在好氧废水处理过程中的成功应用。SPG膜的透气率受其表面润湿性和孔径的影响。疏水膜的透气率优于亲水膜。增大孔径也可提高透气率。在一定的气通量下,DO浓度主要受有机负荷的影响。实验系统基于SPG膜面积的最佳COD去除能力确定为6.88 kg·(m²·d)⁻¹。NH₄⁺-N的去除主要受DO浓度及其在生物膜内扩散的影响。在高有机负荷率下观察到了同步硝化反硝化现象。与传统气泡曝气相比,微气泡曝气中的氧利用效率更高,在最佳运行条件下可能接近100%。

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