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Treatment of tannery wastewater in a pilot-scale hybrid constructed wetland system in Bangladesh 总被引:3,自引:0,他引:3
This paper reports the pollutant removal performances of a hybrid wetland system in Bangladesh for the treatment of a tannery wastewater. The system consisted of three treatment stages: a subsurface vertical flow (VF) wetland, followed by a horizontal flow (HF) and a VF wetland. The wetlands were planted with common reed (Phragmites australis), but employed different media, including organic coco-peat, cupola slag and pea gravel. In the first stage, experimental results demonstrated significant removal of ammonia (52%), nitrate (54%), BOD (78%), and COD (56%) under high organics loading rate (690 g COD m−2 d−1); simultaneous nitrification, denitrification, and organics degradation were attributed to the unique characteristics of the coco-peat media, which allowed greater atmospheric oxygen transfer for nitrification and organic degradation, and supply of organic carbon for denitrification. The second stage HF wetland produced an average PO4 removal of 61%, primarily due to adsorption by the iron-rich cupola slag media. In the third treatment stage, which was filled with gravel media, further BOD removal (78%) from the tannery wastewater depleted organic carbon, causing the accumulation of NO3 in the wastewater. Overall, the average percentage removals of NH3-N, NO3-N, BOD, COD, and PO4 were 86%, 50%, 98%, 98% and 87%, respectively, across the whole hybrid system. The results provided a strong evidence to support widespread research and application of the constructed wetland as a low-cost, energy-efficient, wastewater treatment technology in Bangladesh. 相似文献
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Measuring biomass specific ammonium, nitrite and phosphate uptake rates in aerobic granular sludge 总被引:1,自引:0,他引:1
Aerobic granular sludge (AGS) technology offers the possibility to remove organic carbon, nitrogen and phosphorus in a single reactor system. The granular structure is stratified in such a way that both aerobic and anaerobic/anoxic layers are present. Since most of the biological processes in AGS systems occur simultaneously, the measurement and estimation of the capacity of specific conversions is complicated compared to suspended biomass. The determination of the activities of different functional groups in aerobic granular sludge allows for identification of the potential metabolic capacity of the sludge and aids to analyze bioreactor performance. It allows for comparison of different sludges and enables improved understanding of the interaction and competition between different metabolic groups of microorganisms. The most appropriate experimental conditions and methods to determine specific ammonium, nitrite and phosphate uptake rates under normal operation of AGS reactors were evaluated and described in this study. Extra biomass characterization experiments determining the maximum uptake rate of these compounds on optimized conditions were performed as well to see how much spare capacity was available. The methodologies proposed may serve as an experimental frame of reference for investigating the metabolic capacities of microbial functional groups in biofilm processes. 相似文献
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游离氨对稳定生物亚硝化的影响分析 总被引:12,自引:0,他引:12
在稳定亚硝化期亚硝化菌的竞争优势形成以后,它对FA的变化不是非常敏感,游离氨的作用主要在于提供了一个有利于亚硝化的竞争环境。稳定亚硝化期的两类硝化菌所表现出的反应活性与系统中两类硝化菌在FA抑制环境中竞争所形成的优劣态势关系紧密。将稳定亚硝化期的平均FA浓度维持在7~10mg/L左右是合适的,FA大于15mg/L以后会对亚硝化菌形成抑制。亚硝化系统中即使通过各种途径抑制硝化菌的活性,也不能使其被完全抑制或消除、洗出。当抑制作用减弱或环境条件适宜时硝化菌很快就能恢复活性,杆状絮体是良好亚硝化现象的特征污泥相。 相似文献
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厌氧氨氧化混培菌的获得及其运行条件 总被引:24,自引:0,他引:24
采用了好氧活性污泥和厌氧颗粒污泥混合接种的方法 ,成功地启动了实验室规模的厌氧氨氧化反应器 ,启动后含氨模拟废水运行的进水氨浓度和进水亚硝基氮浓度均为 2 0 mmol/ L ,氨氮、亚硝基氮和总氮的容积负荷率为10 .69mmol/ L·d,12 .2 6mmol/ L· d和 3 94.5 5 mg/ L·d,氨氮、亚硝基氮和总氮的去除率保持在 90 %、99%和 95 %以上 ,对运行条件研究表明 ,厌氧氨氧化反应的最适 p H为 7~ 7.5 ,最适温度约在 3 0± 1℃。厌氧氨氧化随亚硝酸盐浓度的升高而下降 ,氨的厌氧转化随 COD浓度的增加也呈抑制型曲线 ,当 COD浓度为 80 0± 5 0 mg/ L 时 ,厌氧氨氧化速率达到最大 相似文献
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In this study, landfill leachate with and without pre-treatment was co-treated with municipal wastewater at different mixing ratios. The leachate pre-treatment was achieved by air stripping to removal ammonia. The objective of this study was to investigate the effect of landfill leachate on nutrient removal of the wastewater treatment process. It was demonstrated that when landfill leachate was co-treated with municipal wastewater, the high ammonia concentration in the leachate did not have a negative impact on the nitrification. The system was able to adapt to the environment and was able to improve nitrification capacity. The readily biodegradable portion of chemical oxygen demand (COD) in the leachate was utilized by the system to improve phosphorus and nitrate removal. However, this portion was small and majority of the COD ended up in the effluent thereby decreased the quality of the effluent. The study showed that the 2.5% mixing ratio of leachate with wastewater improved the overall biological nutrient removal process of the system without compromising the COD removal efficiency. 相似文献