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首页> 外文期刊>Journal of environmental sciences >Startup and operation of anaerobic EGSB reactor treating palm oil mill effluent
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Startup and operation of anaerobic EGSB reactor treating palm oil mill effluent

机译:厌氧EGSB反应器处理棕榈油厂废水的启动和运行

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摘要

A bench-scale expanded granular sludge bed (EGSB) reactor was applied to the treatment of palm oil mill effluent (POME). The reactor had been operated continuously at 35°C for 514 d,with organic loading rate (OLR) increased from 1.45 to 17.5 kg COD/(m~3 ·d). The results showed that the EGSB reactor had good performance in terms of COD removal on the one hand,high COD removal of 91% was obtained at two days' of hydraulic retention time (HRT),and the highest OLR of 17.5 kg COD/(m~3 ·d). On the other hand,only 46% COD in raw POME was transformed into biogas in which the methane content was about 70% (V/V). A 30-d intermittent experiment indicated that the maximum transformation potential of organic matter in raw POME into methane was 56%. Volatile fatty acid (VFA) accumulation was observed in the later operation stage,and this was settled by supplementing trace metal elements. On the whole,the system exhibited good stability in terms of acidity and alkalinity. Finally,the operational problems inherent in the laboratory scale experiment and the corresponding countermeasures were also discussed.
机译:将台式规模的膨胀式颗粒污泥床(EGSB)反应器用于棕榈油厂废水(POME)的处理。反应器在35°C下连续运转514 d,有机负荷率(OLR)从1.45 kg COD /(m〜3·d)增加到17.5 kg COD /(m〜3·d)。结果表明,EGSB反应器一方面具有良好的COD去除性能,在水力停留时间(HRT)两天时获得了91%的高COD去除率,最高的OLR为17.5 kg COD /( m〜3·d)。另一方面,原始POME中只有46%的COD转化为沼气,其中甲烷含量约为70%(V / V)。 30天的间歇实验表明,原始POME中有机物向甲烷的最大转化潜力为56%。在手术后期观察到挥发性脂肪酸(VFA)的积累,并通过补充微量金属元素来解决。总体而言,该体系在酸度和碱度方面表现出良好的稳定性。最后,还讨论了实验室规模实验固有的操作问题及相应的对策。

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