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Assessment of intermittently loaded woodchip and sand filters to treat dairy soiled water

机译:评估间歇性装填的木屑和砂滤池处理奶场污水的能力

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Land application of dairy soiled water (DSW) is expensive relative to its nutrient replacement value. The use of aerobic filters is an effective alternative method of treatment and potentially allows the final effluent to be reused on the farm. Knowledge gaps exist concerning the optimal design and operation of filters for the treatment of DSW. To address this, 18 laboratory-scale filters, with depths of either 0.6 m or 1 m, were intermittently loaded with DSW over periods of up to 220 days to evaluate the impacts of depth (0.6 m versus 1 m), organic loading rates (OLRs) (50 versus 155 g COD m(-2) d(-1)), and media type (woodchip versus sand) on organic, nutrient and suspended solids (SS) removals. The study found that media depth was important in contaminant removal in woodchip filters. Reductions of 78% chemical oxygen demand (COD), 95% SS, 85% total nitrogen (TN), 82% ammonium-nitrogen (NH4-N), 50% total phosphorus (TP), and 54% dissolved reactive phosphorus (DRP) were measured in 1 m deep woodchip filters, which was greater than the reductions in 0.6 m deep woodchip filters. Woodchip filters also performed optimally when loaded at a high OLR (155 g COD m(-2) d(-1)), although the removal mechanism was primarily physical (i.e. straining) as opposed to biological. When operated at the same OLR and when of the same depth, the sand filters had better COD removals (96%) than woodchip (74%), but there was no significant difference between them in the removal of SS and NH4-N. However, the likelihood of clogging makes sand filters less desirable than woodchip filters. Using the optimal designs of both configurations, the filter area required per cow for a woodchip filter is more than four times less than for a sand filter. Therefore, this study found that woodchip filters are more economically and environmentally effective in the treatment of DSW than sand filters, and optimal performance may be achieved using woodchip filters with a depth of at least 1 m, operated at an OLR of 155 g COD m(-2) d(-1). (C) 2016 Elsevier Ltd. All rights reserved.
机译:相对于其营养价值而言,乳化污水(DSW)在土地上的应用非常昂贵。有氧过滤器的使用是一种有效的替代处理方法,并可能使最终的废水在农场中再利用。在处理DSW的过滤器的最佳设计和操作方面存在知识空白。为了解决这个问题,在长达220天的时间内,对18个深度为0.6 m或1 m的实验室规模的过滤器进行了DSW间歇性加载,以评估深度(0.6 m对1 m),有机加载速率( OLRs(50 vs 155 g COD m(-2)d(-1)),以及去除有机物,营养物和悬浮固体(SS)的介质类型(木片vs沙子)。研究发现,介质深度对于木屑过滤器中的污染物去除很重要。减少78%的化学需氧量(COD),95%的SS,85%的总氮(TN),82%的铵氮(NH4-N),50%的总磷(TP)和54%的溶解性活性磷(DRP) )是在1 m深的木片过滤器中测得的,这比0.6 m深的木片过滤器的减少量要大。尽管去除机理主要是物理的(即过滤)而不是生物学的,但在高OLR(155 g COD m(-2)d(-1))加载时,木屑过滤器的性能也最佳。在相同的OLR和相同的深度下操作时,砂滤池的COD去除率(96%)比木屑(74%)更好,但是在去除SS和NH4-N方面它们之间没有显着差异。但是,堵塞的可能性使沙滤器不如木屑过滤器理想。使用两种配置的最佳设计,木片过滤器每头牛所需的过滤器面积是沙滤器的四倍多。因此,本研究发现木屑过滤器在处理DSW方面比沙滤器更加经济和环保,并且使用深度至少为1 m的木屑过滤器(在155 g COD m的OLR下运行)可以实现最佳性能。 (-2)d(-1)。 (C)2016 Elsevier Ltd.保留所有权利。

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