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Anaerobic treatment of oil-contaminated wastewater with methane production using anaerobic moving bed biofilm reactors

机译:使用厌氧移动床生物膜反应器厌氧处理甲烷产生的含油废水

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Oil-contaminated wastewaters are generally treated by a combination of physico-chemical and biological methods. Interest in the anaerobic treatment of oily wastewaters has increased since it complements aerobic treatment and produces energy in the form of methane. The objectives of this study were to characterise the anaerobic process spontaneously occurring in a full-scale storage tank at a facility treating waste oil and oil-contaminated effluents, and to evaluate the applicability of an anaerobic moving bed biofilm reactor (AnMBBR) and an anaerobic contact reactor (ACR) for treating the oil contaminated wastewater feeding the storage tank. Three lab-scale reactors were operated in parallel over 465 days: one mesophilic and one thermophilic AnMBBR, and one thermophilic ACR. The wastewater had a high strength with an average chemical oxygen demand (COD) of 36 g/L with a soluble fraction of 80%. The BOD7/COD ratios varied between 0.1 and 0.5, indicating low aerobic degradability. However, biomethane potential tests indicated some level of anaerobic degradability with methane yields between 150 and 200 NmL/gCOD. The full-scale storage tank operated at low organic loading rates (0.35-0.43 kgCOD/m(3)d), and long hydraulic retention times (HRT = 83-104 d). In comparison, the AnMBBRs achieved similar COD reductions (60%) as the full-scale tank but at a much shorter HRT of 30 d. Similar efficiency could only be reached at longer HRTs (43 d) in the ACR due to low biomass levels resulting from poor sludge settleability. The methane yield was higher (210 NmLCH(4)/COD removed) in the AnMBBR operated at 37 degrees C, compared to the other reactors working at 50 degrees C (180 NmLCH(4)/COD removed). This reactor also maintained a higher COD removal (67%) at an increased OLR of 1.1 kgCOD/m(3)d than the AnMBBR at 50 degrees C. The microbial composition of the biomass from the full-scale tank and the laboratory reactors provided evidence for the conversion of oil-contaminated wastewater into methane with a relatively high abundance of hydrogenotrophic methanogens. (C) 2019 Published by Elsevier Ltd.
机译:受油污染的废水通常通过物理化学和生物方法相结合的方法进行处理。对含油废水进行厌氧处理的兴趣有所增加,因为它补充了好氧处理并产生甲烷形式的能量。这项研究的目的是表征在处理废油和受油污染的废水的设施的大型储罐中自发发生的厌氧过程,并评估厌氧移动床生物膜反应器(AnMBBR)和厌氧的适用性接触反应器(ACR),用于处理送入储油罐的被油污染的废水。三个实验室规模的反应器在465天里并行运行:一个中温和一个嗜热AnMBBR,一个热解ACR。废水强度高,平均化学需氧量(COD)为36 g / L,可溶性分数为80%。 BOD7 / COD比在0.1到0.5之间变化,表明有氧降解能力低。但是,生物甲烷潜力测试表明厌氧降解能力达到一定水平,甲烷产量在150至200 NmL / gCOD之间。全尺寸储罐在低有机负荷率(0.35-0.43 kgCOD / m(3)d)和长水力停留时间(HRT = 83-104 d)下运行。相比之下,AnMBBR的COD减少量与全尺寸水箱相似(60%),但HRT短得多(30 d)。由于污泥沉降性差而导致生物量水平较低,因此只有在较长的HRT(43 d)中才能达到类似的效率。与在50摄氏度下工作的其他反应器(除去180 NmLCH(4)/ COD)相比,在37摄氏度下运行的AnMBBR的甲烷收率更高(除去210 NmLCH(4)/ COD)。该反应器在50摄氏度下的OLR增加到1.1 kgCOD / m(3)d时,还保持了较高的COD去除率(67%),高于AnMBBR。提供了全尺寸水箱和实验室反应器中的生物量有证据表明,石油污染的废水转化为甲烷并具有相对较高的氢营养型产甲烷菌。 (C)2019由Elsevier Ltd.发布

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