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Process optimization and energy analysis of vacuum degasifier systems for the simultaneous removal of dissolved methane and hydrogen sulfide from anaerobically treated wastewater

机译:真空脱气系统的处理优化和能量分析,用于同时除去厌氧处理废水的溶解甲烷和硫化氢

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The control of dissolved methane (CH4) and hydrogen sulfide (H2S) emissions in anaerobic effluents is essential for minimizing the environmental implications of greenhouse gases, odor, and carbon footprint, as well as for preventing energy loss in the form of unrecovered dissolved methane. This study assessed the feasibility of a vacuum degasifier for the removal of CH4 and H2S from staged anaerobic fluidized membrane bioreactor (SAF-MBR) effluent. The optimization results showed that the efficiency of the nozzle fitted degasifiers were superior to the media packed ones. In three-stage vacuum degasifiers at a -0.8 bar vacuum pressure, H2S removal was mostly pH dependent and 88% removal efficiency was achieved with an initial concentration of 13.6 mg/L. Methane removal was dependent primarily on the number of degasifier units, and approximately 94% efficiency was achieved in a three-stage degasifier. Energy balance analysis showed that energy production exceeded the system energy requirements with 0.05-0.07 kWh/m(3) of surplus energy. These results provide deep insights into this new technology for simultaneous removal of dissolved CH4 and H2S, which can be referred for potential future applications. (C) 2020 Elsevier Ltd. All rights reserved.
机译:厌氧流出物中溶解甲烷(CH 4)和硫化氢(H2S)排放的控制对于最小化温室气体,气味和碳足迹的环境影响,以及防止未折叠的溶解甲烷的形式的能量损失至关重要。该研究评估了真空涂料的可行性,用于从分段的厌氧流化膜生物反应器(SAF-MBR)流出物中除去CH 4和H 2。优化结果表明,喷嘴所脱气剂的效率优于介质包装络合物。在-0.8巴的三级真空脱气机中,H 2 S除去主要是pH依赖性,并且初始浓度为13.6mg / L.甲烷除去主要依赖于脱气器单元的数量,在三级脱气器中实现了大约94%的效率。能量平衡分析表明,能源产量超过了系统能源要求,0.05-0.07千瓦时/ m(3)剩余能量。这些结果对这种新技术提供了深入的见解,同时去除溶解的CH4和H2S,可以提及潜在的未来应用。 (c)2020 elestvier有限公司保留所有权利。

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