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The effect of various iron hydroxide concentrations on the anaerobic fermentation of sulfate-containing model wastewater

机译:各种氢氧化铁浓度对含硫酸盐模型废水厌氧发酵的影响

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The addition of iron hydroxide and iron-reducing bacteria into a reactor for anaerobic processing of sulfate-containing wastewater was shown to decrease sulfate reduction and sulfide concentration, while increasing the total organic carbon (TOC) and methane production. The effect of iron (III) in sulfate-containing wastewater depended on its dose, which can be expressed as molar ratio Fe(III)/SO 4 2? . Sulfide concentration increased monotonically, reaching 91 and 45 mg/l after 15 days of processing at Fe(III)/SO 4 2? ratios of 0.06 and 0.5, respectively. However, soluble sulfide production was not observed at ratios equaling 1 and 2. At ratios of 0.06, 0.5, 1, and 2, the maximum rates of TOC removal were 0.75, 1.15, 1.39, and 1.55 g TOC/g of organic matter (OM) per 1 h. Methane production rates were 0.039, 0.047, 0.064, and 0.069 ml/g OM per 1 h, with the mean relative amounts of methane in the biogas being equal to 25, 41, 55, and 62%, respectively. These data can be applied to the development of new methods of anaerobic purification of sulfate-containing wastewater.
机译:结果表明,向反应器中添加氢氧化铁和还原铁细菌进行含硫酸盐废水的厌氧处理可减少硫酸盐的还原和硫化物的浓度,同时增加总有机碳(TOC)和甲烷的产量。铁(III)在含硫酸盐废水中的作用取决于其剂量,可以用Fe(III)/ SO 42α的摩尔比表示。 。在Fe(III)/ SO 4 2?处理15天后,硫化物浓度单调增加,达到91和45 mg / l。比分别为0.06和0.5。然而,在比率等于1和2时未观察到可溶性硫化物的产生。比率为0.06、0.5、1和2时,TOC去除的最大速率为0.75、1.15、1.39和1.55 g TOC / g有机物( OM)每1小时。甲烷生产速率为每1小时0.039、0.047、0.064和0.069 ml / g OM,沼气中甲烷的平均相对量分别等于25%,41%,55%和62%。这些数据可用于厌氧净化含硫酸盐废水的新方法的开发。

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