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The effect of sulfide inhibition and organic shock loading on anaerobic biofilm reactors treating a low-temperature, high-sulfate wastewater

机译:硫化物抑制和有机冲击负荷对厌氧生物膜反应器处理低温高硫酸盐废水的影响

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摘要

In order to assess the long-term treatment of sulfate- and carbon- rich wastewater at low temperatures, three anaerobic biofilm reactors were operated at 20°C, a hydraulic retention time (HRT)of two days and fed a synthetic wastewater containing lactate and sulfate. The reactors were operated for over 900 days. DNA was extracted from the reactors around days 180 and 800. Three clone libraries, methanogenic archaea (MA), sulfate reducing bacteria (SRB), and bacteria, were constructed and quantitative PCR analysis was performed with the DNA. It was found that anaerobic biofilm reactors can be operated at 20°C with an organic load rate (OLR) of 1.3 g-chemical oxygen demand (COD)/L-day or less and an sulfur load rate (SLR) of 0.2 g-S/L-day with no significant deterioration in process performance. With long acclimation periods, OLR as high as 3.4 g COD/L-d and SLR of 0.3 g/L-d can be tolerated, producing effluent volatile-acid COD levels consistently less than 200 mg/L. Effluent dissolved sulfide and hydrogen sulfide levels were around 600 mg S/L and 150 mg S/L, respectively, during this period. In addition to long term operation, the effect of organic shock loading was assessed. The reactors were able to recover from one but not two lactate spikes of approximately 5,000 mg COD/L. It was determined that long-term stability could be achieved in reactors that contained well balanced, stable populations of lactate- and propionate-degrading SRB and aceticlastic methanogens. Significant populations of fermenters present resulted in an imbalance which caused lactate to be routed through an additional pathway where propionate was formed. Greater numbers of MA than bacteria were found in all reactors. This may be attributed to the availability of acetate in the reactors for MA consumption and to using the immobilized fixed bed reactor type. Aceticlastic methanogens were the dominant methanogen, and were observed to remove nearly all acetate produced in all reactors. SRB were observed to remove lactate in microbially balanced reactors, whereas fermenters degraded lactate in reactors with less balanced populations.
机译:为了评估低温下富含硫酸盐和碳的废水的长期处理,三个厌氧生物膜反应器在20°C,水力停留时间(HRT)为两天的条件下运行,并向其中添加了含乳酸和水的合成废水。硫酸盐。反应器运行900天以上。在第180和800天左右从反应器中提取DNA。构建了三个克隆文库,产甲烷菌(MA),硫酸盐还原细菌(SRB)和细菌,并对DNA进行了定量PCR分析。发现厌氧生物膜反应器可以在20°C下运行,有机负荷率(OLR)为1.3克化学需氧量(COD)/ L天或更小,硫负荷率(SLR)为0.2 gS / L天,工艺性能无明显下降。在较长的适应时间下,可以耐受高达3.4 g COD / L-d的OLR和0.3 g / L-d的SLR,产生的废水中挥发性酸的COD水平始终低于200 mg / L。在此期间,废水中溶解的硫化物和硫化氢水平分别约为600 mg S / L和150 mg S / L。除长期操作外,还评估了有机冲击负荷的影响。反应器能够从大约5,000 mg COD / L的一个而不是两个乳酸峰中回收。可以确定,在那些反应平衡良好,稳定的降解乳酸和丙酸酯的SRB和乙酰弹性产甲烷菌的反应堆中,可以实现长期稳定性。存在的大量发酵罐导致失衡,导致乳酸通过形成丙酸酯的另一途径进行转运。在所有反应堆中发现的MA数量均大于细菌数量。这可能归因于反应器中乙酸盐可用于MA消耗以及使用固定式固定床反应器类型。乙炔型产甲烷菌是主要的产甲烷菌,据观察,它几乎清除了所有反应器中产生的所有乙酸盐。观察到SRB在微生物平衡的反应器中去除了乳酸,而发酵罐在平衡性较低的反应器中降解了乳酸。

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  • 作者

    McDonald, Heather Brown;

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  • 年度 2007
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  • 原文格式 PDF
  • 正文语种 eng
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