首页> 外文期刊>Journal of Environmental Science and Health. A, Toxic/Hazardous Substances & Environmental Engineering >Synthetic Dairy Wastewater Treatment Using a New Horizontal-Flow Biofilm Reactor
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Synthetic Dairy Wastewater Treatment Using a New Horizontal-Flow Biofilm Reactor

机译:使用新型水平流生物膜反应器处理合成乳品废水

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The aim of this study was to develop a simple biological system that would be suitable for the treatment of dairy parlour wash waters. A novel horizontal-flow biofilm system was designed, constructed and tested in the laboratory for organic carbon and nitrogen removal from a synthetic dairy wastewater with average filtered chemical oxygen demand (COD_f) of 2947.7 mg/L and total nitrogen (TN) of 295.5 mg/L. The novel biofilm system consisted of two reactor units one on top of the other. Each reactor unit comprised a stack of horizontal plastic sheets placed above one another that were supported and separated by vertical plastic cone frustums, which were formed in the sheets during manufacture. The wastewater was pumped onto the top sheet of the top reactor unit at hourly intervals for a 5-minute period and flowed over and back along alternate sheets down through the 2 units. The top unit had 8 plastic sheets and 25 mm high frustums to cater for heavy biofilm growth, and the bottom unit had 17 sheets and 11 mm high frustums for thinner biofilm growth. The organic loading of 57 g COD_f/m~2 · d—based on the plan area of the system—was applied to the top reactor unit. When the reactor process reached pseudo steady-state, about 96% COD_f, 71% TN and 100% ammonium nitrogen were removed. Low solids production occurred. The system was simple and easy to construct and operate.
机译:这项研究的目的是开发一种简单的生物系统,适用于乳制品店洗手水的处理。在实验室中设计,构建和测试了新型水平流生物膜系统,用于从合成奶场废水中去除有机碳和氮,平均过滤化学需氧量(COD_f)为2947.7 mg / L,总氮(TN)为295.5 mg /升新颖的生物膜系统由两个反应器单元组成,一个位于另一个之上。每个反应器单元包括一叠水平的塑料板,这些塑料板彼此叠置,并由垂直的塑料圆锥形截头锥体支撑并分开,这些圆锥形的截头锥体在制造过程中形成在板中。每小时以5分钟的时间间隔将废水泵送到顶部反应器单元的顶板上,然后沿着交替的板上下流动通过2个单元。顶部单元具有8个塑料薄片和25mm高的平截头体,以适应较厚的生物膜生长,而底部单元具有17个薄片和11mm高的平截头体,以实现较薄的生物膜生长。根据系统的计划面积,将57 g COD_f / m〜2·d的有机负荷应用于顶部反应器单元。当反应器过程达到拟稳态时,除去约96%的COD_f,71%的TN和100%的铵氮。固体产量低。该系统非常简单,易于构建和操作。

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