Improving the efficiency of small-scale wastewater treatment by pneumatic agitation

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dc.contributor.author Sun, Shaohua
dc.contributor.author Tong, Yanming
dc.contributor.author Hou, Aiying
dc.contributor.author Yin, Lijun
dc.contributor.author Zheng, Tong
dc.contributor.author Zheng, Jie
dc.contributor.author Liu, Jicheng
dc.contributor.author Cao, Bing
dc.contributor.author Hu, Qing
dc.contributor.author Coulon, Frederic
dc.contributor.author Yang, Xiao Jin
dc.date.accessioned 2022-01-13T10:40:45Z
dc.date.available 2022-01-13T10:40:45Z
dc.date.issued 2021-12-23
dc.identifier.citation Sun S, Tong Y, Hou A, et al., (2022) Improving the efficiency of small-scale wastewater treatment by pneumatic agitation, Environmental Technology and Innovation, Volume 26, May 2022, Article number 102220 en_UK
dc.identifier.issn 2352-1864
dc.identifier.uri https://doi.org/10.1016/j.eti.2021.102220
dc.identifier.uri http://dspace.lib.cranfield.ac.uk/handle/1826/17407
dc.description.abstract Small-scale anaerobic and aerobic systems for wastewater treatment suffer relatively low efficiencies due primarily to a lack of mechanical agitation/mixing. Here, a pneumatic agitation system was designed by installing a U-tube between the anaerobic and anoxic units, pumping air to the closed headspace of the anaerobic unit and releasing the pressurized air through the U-tube to create turbulence of the fluid. Computational Fluid Dynamics (CFD) simulation and fluid tracer trial were used to describe the fluid status in a lab-scale system (13 L). The results demonstrated that a continuous 5-cycle pneumatic agitation achieved a complete mixing of the static fluid. The retention time factor () and short-circuiting flow coefficient (/HRT) were increased from 0.93 to 1.14 and 0.02 to 0.27, respectively, indicating that pneumatic agitation significantly reduced dead zone and short-circuiting flow. A prototype at a treatment capacity of 300 L/d was installed in the North-East suburb of Beijing (40.15° N, 116.95° E) to treat rural household wastewater consisting of 630–1200 mg/L chemical oxygen demand and 20–45 mg/L total nitrogen. The field test was monitored in a period of 75 days from September to November 2018. The average removal rate for COD and TN was 96% and 92%, respectively by 10 times/h pneumatic agitation as compared to 49% and 45% without pneumatic agitation. The pneumatic agitation provides a low cost, easy operation and maintenance and efficient means for small-scale domestic wastewater treatment. en_UK
dc.language.iso en en_UK
dc.publisher Elsevier en_UK
dc.rights Attribution-NonCommercial-NoDerivatives 4.0 International *
dc.rights.uri http://creativecommons.org/licenses/by-nc-nd/4.0/ *
dc.subject Domestic wastewater treatment en_UK
dc.subject Small-scale en_UK
dc.subject Pneumatic agitation en_UK
dc.subject Chemical oxygen demand en_UK
dc.subject Total nitrogen en_UK
dc.title Improving the efficiency of small-scale wastewater treatment by pneumatic agitation en_UK
dc.type Article en_UK


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