AnoxKaldnes, Veolia Water Technologies AB, Klosterängsvägen 11a, 226 47, Lund, Sweden.
AnoxKaldnes, Veolia Water Technologies AB, Klosterängsvägen 11a, 226 47, Lund, Sweden; Swedish Centre for Resource Recovery, University of Borås, 501 90, Borås, Sweden.
Water Res. 2019 Oct 15;163:114851. doi: 10.1016/j.watres.2019.07.018. Epub 2019 Jul 11.
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 BOD/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/md), 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/COD removed) in the AnMBBR operated at 37 °C, compared to the other reactors working at 50 °C (180 NmLCH/COD removed). This reactor also maintained a higher COD removal (67%) at an increased OLR of 1.1 kgCOD/md than the AnMBBR at 50 °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.
含油废水通常采用物理化学和生物方法的组合进行处理。由于厌氧处理可以补充好氧处理,并以甲烷的形式产生能源,因此人们对含油废水的厌氧处理越来越感兴趣。本研究的目的是对处理废油和含油废水的设施中的一个大型储存罐中自然发生的厌氧过程进行特征描述,并评估厌氧移动床生物膜反应器(AnMBBR)和厌氧接触反应器(ACR)在处理储存罐进料中含油污染废水的适用性。在 465 天的时间里,三个实验室规模的反应器平行运行:一个中温和一个高温 AnMBBR,和一个高温 ACR。废水具有高浓度,平均化学需氧量(COD)为 36g/L,可溶部分为 80%。BOD/COD 比值在 0.1 到 0.5 之间,表明好氧降解性低。然而,生物甲烷潜力测试表明存在一定程度的厌氧降解性,甲烷产率在 150 到 200 NmL/gCOD 之间。大型储存罐以低有机负荷(0.35-0.43 kgCOD/md)和长水力停留时间(HRT=83-104d)运行。相比之下,AnMBBR 以较短的 30d HRT 实现了与大型储罐相似的 COD 去除率(60%)。由于污泥沉降性能差导致生物量水平低,仅在较长的 HRT(43d)下才能在 ACR 中达到相似的效率。在 37°C 下运行的 AnMBBR 的甲烷产量较高(210 NmLCH/COD 去除),而在 50°C 下运行的其他反应器的甲烷产量为 210 NmLCH/COD 去除)。该反应器在 1.1 kgCOD/md 的较高 OLR 下也保持了较高的 COD 去除率(67%),高于 50°C 下的 AnMBBR。来自大型储罐和实验室反应器的生物量的微生物组成提供了将含油废水转化为甲烷的证据,其中氢营养型产甲烷菌的相对丰度较高。