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首页> 外文期刊>International Journal of Environmental Science and Technology >Inoculum-free start-up of biofilm- and sludge-based deammonification systems in pilot scale
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Inoculum-free start-up of biofilm- and sludge-based deammonification systems in pilot scale

机译:在飞行员规模的生物膜和基于污泥的污泥的脱泥系统的自由造型

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Undiluted reject water from the dewatering of anaerobic sludge with an average total nitrogen content of 718 +/- 117 mg L-1 (n = 63) was used to start-up autotrophic nitrogen removal in three different pilot-scale (3 m(3)) deammonification configurations: (1) biofilm; (2) activated sludge sequence batch; and (3) two-staged (nitritation-anammox). Time- and concentration-based aeration control with alternating aerobic/anaerobic phases was applied for all reactor configurations. All reactors were initiated without anammox-specific inoculum, and biofilm was grown onto blank carriers. During the initial start-up period, biological nitrogen removal was found to be inhibited by an excessive free ammonia content ( 10 mg-N L-1), resulting from the use of high-strength reject water as the process feed. After implementation of free ammonia control by pH adjustment to 6.5-7.5, propagation of the deammonification process was observed with increased nitrogen removal with slight accumulation of NO3 (-)-N. The highest total nitrogen removal rates were achieved with the single-reactor biofilm- and sludge-based deammonification processes (1.04 and 0.30 kg-N m(-3) day(-1), respectively). The critical factors for successful start-up and stable operation of deammonification reactors turned out to be control of pH below 7.5, dissolved oxygen at 0.3-0.8 mg-O-2 L-1 and influent solids values below 1000 nephelometric turbidity units. Microbial analysis demonstrated that highest anammox enrichment was achieved in the biofilm reactor (9.40 x 10(8) copies g(-1) total suspended solids). These data demonstrate the potential of an in-situ grown sludge- or biofilm-based concept for the development and propagation of deammonification process.
机译:来自厌氧污泥的脱水的未稀释的废水,平均总氮含量为718 +/- 117mg L-1(n = 63),用于以三种不同的先导级(3米(3) ))Deammonification Conculationations:(1)生物膜; (2)活性污泥序列批量; (3)双分阶段(硝酸盐 - 厌氧毒剂)。所有反应器配置施加具有交替的有氧/厌氧相的时间和浓度的曝气控制。所有反应器都是在没有厌氧毒素的接种物中引发的,并且生物膜生长到坯料载体上。在初始启动期间,发现生物氮去除通过过量的游离氨含量(& 10mg-n L-1)抑制,由使用高强度废水作为过程进料来抑制。通过pH调节将自由氨对照实施至6.5-7.5后,观察到脱氮过程的繁殖,随着NO3( - ) - n的轻微积累而增加的氮气去除。用基于单反应器生物膜和污泥的脱泥化方法(1.04和0.30kg-N m(-3)天(-1),实现了最高的氮去除率。成功启动和稳定操作的关键因素对脱模反应器的稳定运行,对pH的控制进行控制,在7.5以下,溶解氧在0.3-0.8mg-O-2 L-1和低于1000个浊度浊度单元以下的水中值。微生物分析表明,在生物膜反应器中实现了最高的厌氧氧富集(9.40×10(8)拷贝G(-1)总悬浮固体)。这些数据表明了原位生长的污泥或基于生物膜的概念的潜力,用于脱模过程的开发和繁殖。

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