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Sulfur balance in the treatment of sulfur-containing wastewater in a biotrickling reactor

机译:在生物轧制反应器中处理含硫废水的硫平衡

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Biological sulfite reduction was studied in a laboratory-scale anaerobic biotrickling reactor packed with ceramic granule for biomass attachment. Inoculated with the Sulfate-reducing Bacteria isolated from landfill leachate, the reactor was operated for 72h per cycle at room temperature with a sulfite loading rate of 1360 mg/L. The sulfite removal efficiency reached 97% after 9.5h. However, the total sulfur and Chemical Oxygen Demand (COD) reduction were 40% and 48.2% respectively at that time. To quantify various sulfur speciations, calculation of sulfur balance was performed, which revealed that up to 76% of sulfite removed was converted to elemental sulfur. In addition, the Oxidation-reduction potential (ORP) maintained within the range of −61mv to −20mv, which is different from the widely reported value: lower than −100mv. It is effective to treat sulfur-contining waste water using biotrckling reactor.
机译:研究了生物亚硫酸盐还原,在实验室型厌氧生物轧制反应器中填充有陶瓷颗粒的生物质附着。接种从垃圾渗滤液中分离的硫酸盐还原细菌,在室温下每循环运转反应器72小时,亚硫酸盐加载速率为1360mg / L. 9.5h后亚硫酸盐去除效率达到97%。然而,当时,总硫和化学需氧量(COD)减少分别为40%和48.2%。为了量化各种硫的凝版,进行硫平衡的计算,表明,除去76%的亚硫酸盐转化为元素硫。此外,氧化还原电位(ORP)保持在-61mV至-20mV的范围内,这与广泛报道的值不同:低于-100mV。使用生物曲线反应器治疗硫延续废水是有效的。

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