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Optimization of the Simultaneous Removal of Nitrogen and Organic Matter from Fishery Wastewaters

机译:从渔业废水中同时去除氮和有机质的优化

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Anaerobic treatment of saline and protein-rich effluents reduces the organic concentration but forms ammonium that hinders nitrogen removal in a later aerobic treatment. The goal of this work was to optimize the design of a denitrifying-nitrifying system for the simultaneous removal of organic matter and nitrogenous compounds from fishery effluents to meet the Chilean legal standards and to compare pre- and post-denitrification processes in the biological treatment of high-strength effluents to minimize the total volume of biological reactors required. A predenitrifying system, that included three reactors—acidifying anaerobic filter, denitrifying (anoxic) filter, and aerobic-active sludge (nitrifying reactor) with recycle to the denitrifying reactor—reduced nitrogen to 0.33 g of total ammonia nitrogen (TAN) L~(-1) well above the allowed 0.05 g total nitrogen L~(-1). The predenitrifying system with a second denitrifying reactor, to which organic matter was added, met the legal organic matter and nitrogen emission concentrations (0.042 g TAN L~(-1)). Conversions were 99.0, 92.5, 90.9, and 99.0% for the anaerobic digestion, first denitrification, nitrification, and second denitrification, respectively.
机译:盐水和富含蛋白质的废水的厌氧处理降低了有机物的浓度,但形成了铵,阻碍了后来的需氧处理中氮的去除。这项工作的目的是优化反硝化-硝化系统的设计,以同时从渔业废料中去除有机物和含氮化合物,以达到智利的法律标准,并比较脱氮前和后的脱氮过程在生物处理中的应用。高强度废水可最大程度地减少所需的生物反应器的总体积。包括三个反应器(酸化厌氧过滤器,反硝化(厌氧)过滤器和好氧活性污泥(硝化反应器),并循环至反硝化反应器)的预反硝化系统将氮还原为0.33 g总氨氮(TAN)L〜( -1)远高于允许的总氮0.05 g L〜(-1)。带有第二个反硝化反应器的预硝化系统,其中添加了有机物,符合法定有机物和氮的排放浓度(0.042 g TAN L〜(-1))。厌氧消化,第一次反硝化,硝化和第二次反硝化的转化率分别为99.0%,92.5、90.9和99.0%。

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