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

机译:生物滴流反应器中含硫废水处理中的硫平衡

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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:在实验室规模的厌氧生物滴流反应器中研究了生物亚硫酸盐的还原,该反应器装有陶瓷颗粒以附着生物质。用从垃圾渗滤液中分离出的硫酸盐还原菌接种后,该反应器在室温下每个循环运行72h,亚硫酸盐负载率为1360 mg / L。 9.5小时后,亚硫酸盐去除率达到97%。但是,当时的总硫和化学需氧量(COD)减少分别为40%和48.2%。为了量化各种硫形态,进行了硫平衡的计算,结果表明,除去的亚硫酸盐中多达76%转化为元素硫。另外,氧化还原电位(ORP)维持在-61mv至-20mv的范围内,这与广泛报道的值不同:低于-100mv。使用生物trtrling反应器来处理含硫的废水是有效的。

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