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首页> 外文期刊>Journal of the Serbian Chemical Society >Fenton process combined with precipitation for the removal of Direct Blue 1 dye: A new approach
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Fenton process combined with precipitation for the removal of Direct Blue 1 dye: A new approach

机译:芬顿过程结合沉淀去除直接蓝1染料:一种新方法

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Azo dyes are recalcitrant pollutants present in effluents of several industries. Due to their chemical stability, their degradation efficiency is not satisfactory by conventional technologies. Advanced oxidation processes, such as Fenton, can be applied for the removal of recalcitrant compounds. However, these methods are still costly. In this work, Fenton and precipitation treatments were combined for the removal (i.e., decolorization) of direct blue 1 (DB1), as an option to decrease operational costs. The individual treatments were studied separately using DB1 solutions 0.04 mmol L-1 to determine the effects of the parameters involved in each process. For the Fenton treatment, the c(Fe2+):c(H2O2) ratio that allowed the highest DB1 decolorization was 1:40. Regarding precipitation, the highest dye decolorization was achieved at a pH value of 6.0. Moreover, it was determined that a minimum c(DB1):c(Fe2+) ratio of 1:7.7 is needed to allow the decolorization of the dye by precipitation. Fenton assisted with precipitation tests were performed with DB1 solutions 0.09 mmol L-1 and using a c(DB1):c(Fe2+) ratio of 1:7.3 (which allows only partial precipitation of DB1). The results suggested that the dye can be treated by a Fenton process for 5 min and then precipitated to achieve the almost total decolorization of the dye (97.79 %). Azo dyes are recalcitrant pollutants present in effluents of several industries. Due to their chemical stability, their degradation efficiency is not satisfactory by conventional technologies. Advanced oxidation processes, such as Fenton, can be applied for the removal of recalcitrant compounds. However, these methods are still costly. In this work, Fenton and precipitation treatments were combined for the removal (i.e., decolorization) of direct blue 1 (DB1), as an option to decrease operational costs. The individual treatments were studied separately using DB1 solutions 0.04 mmol L-1 to determine the effects of the parameters involved in each process. For the Fenton treatment, the c(Fe2+):c(H2O2) ratio that allowed the highest DB1 decolorization was 1:40. Regarding precipitation, the highest dye decolorization was achieved at a pH value of 6.0. Moreover, it was determined that a minimum c(DB1):c(Fe2+) ratio of 1:7.7 is needed to allow the decolorization of the dye by precipitation. Fenton assisted with precipitation tests were performed with DB1 solutions 0.09 mmol L-1 and using a c(DB1):c(Fe2+) ratio of 1:7.3 (which allows only partial precipitation of DB1). The results suggested that the dye can be treated by a Fenton process for 5 min and then precipitated to achieve the almost total decolorization of the dye (97.79 %).
机译:偶氮染料是若干行业的污染物中存在的醋酸污染物。由于它们的化学稳定性,其降解效率不受常规技术令人满意的。可以施加先进的氧化方法,例如FENTON,用于去除核批准的化合物。但是,这些方法仍然昂贵。在这项工作中,将芬顿和沉淀处理组合用于直接蓝1(DB1)的去除(即脱色),作为降低运营成本的选择。使用DB1溶液分别研究单独的处理0.04mmol L-1,以确定每个过程中涉及的参数的效果。对于芬顿治疗,允许最高DB1脱色的C(Fe2 +):C(H2O2)比率为1:40。关于沉淀,在pH值为6.0的pH值下实现最高染料脱色。此外,确定最小C(DB1):C(Fe2 +)比率为1:7.7,以通过沉淀脱色染料。用DB1溶液辅助沉淀试验的FENTON与DB1溶液进行0.09mmol L-1,使用C(DB1):C(FE2 +)比为1:7.3(仅允许DB1的部分沉淀)。结果表明,染料可以通过FENTON工艺处理5分钟,然后沉淀,以达到染料的几乎全脱光(97.79%)。偶氮染料是若干行业的污染物中存在的醋酸污染物。由于它们的化学稳定性,其降解效率不受常规技术令人满意的。可以施加先进的氧化方法,例如FENTON,用于去除核批准的化合物。但是,这些方法仍然昂贵。在这项工作中,将芬顿和沉淀处理组合用于直接蓝1(DB1)的去除(即脱色),作为降低运营成本的选择。使用DB1溶液分别研究单独的处理0.04mmol L-1,以确定每个过程中涉及的参数的效果。对于芬顿治疗,允许最高DB1脱色的C(Fe2 +):C(H2O2)比率为1:40。关于沉淀,在pH值为6.0的pH值下实现最高染料脱色。此外,确定最小C(DB1):C(Fe2 +)比率为1:7.7,以通过沉淀脱色染料。用DB1溶液辅助沉淀试验的FENTON与DB1溶液进行0.09mmol L-1,使用C(DB1):C(FE2 +)比为1:7.3(仅允许DB1的部分沉淀)。结果表明,染料可以通过FENTON工艺处理5分钟,然后沉淀,以达到染料的几乎全脱光(97.79%)。

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