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Design Aspects of a Continuous Flow Photocatalytic Reactor and its Application to Degrade Methylene Blue and Textile Wastewater

机译:Design Aspects of a Continuous Flow Photocatalytic Reactor and its Application to Degrade Methylene Blue and Textile Wastewater

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摘要

A continuous flow photocatalytic reactor was developed by combining the reaction kinetics and mass balance concept. The concept of cascade aerator was also considered in designing it as a stepped reactor. The reactor was used to investigate the photocatalytic degradation of methylene blue in aqueous solution by Ag~+ doped TiO2 (2 g/L) under UV irradiation by 15 W UV lamps (254 nm). Methylene blue solution (20 ppm) was found to be decolorized by >99, 97, 85 and 57% under flow rates of 1, 1.5, 2 and 3 L/h, respectively after 120 minutes. The corresponding mineralization was >80, 78, 75 and 54%, respectively. At higher flow rates (Re number 208.2 and 415.5) >99% decolourization was achieved by recycling the solution 5 and 7 times with fresh doses of photocatalyst. At steady state, maintained by repeating the addition of photocatalyst at fixed time intervals, the dye solution could be decolourized continuously by >99, 97 and 76% at flow rates of 1, 2 and 3 L/h, respectively while the mineralization was >82, 79 and 62%, respectively. The reactor was also effectively used to mineralize textile wastewater collected from a textile mill in Kolkata. The mineralization was greater than 75, 73 and 64% at flow rates of 1, 2 and 3 L/h, respectively after 120 minutes. The efficiency of the reactor depended upon the residence time of the contaminant in the reactor. At steady state, the design data simulated well with the corresponding experimental data.
机译:光催化反应器连续流由结合反应动力学和开发质量平衡的概念。增氧机也认为它作为一个设计加强反应堆。调查的光催化降解亚甲蓝溶液的Ag) ~ +掺杂在紫外光照射下二氧化钛(2 g / L) 15 W紫外灯(254海里)。被发现使脱色99年>,97年,85年57%的流速下1、1.5、2和3 L / h,分别在120分钟。矿化> 80、78、75和54%,分别。208.2和415.5)> 99%脱色通过回收解决方案5和7次用新鲜的剂量的光催化剂。状态,由重复添加光催化剂在固定时间间隔,染料解决方案可以连续漂白> 99年、97年和76%流量的1、2和3 L / h,分别在矿化> 82,79和62%,分别。有效地用于采集矿物纺织废水收集从一个纺织厂在加尔各答。矿化是大于75,73和64%流量的1、2和3 L / h,分别120分钟。依赖的停留时间污染物的反应堆。设计数据和相应的模拟得很好实验数据。

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  • 来源
    《Chemistry Select》 |2022年第38期|共8页
  • 作者单位

    Department of Civil Engineering Indira Gandhi Institute of Technology Sarang,Dhenkanal Odisha India-759146;

    Department of Chemistry Indira Gandhi Institute of Technology Sarang,Dhenkanal Odisha India-759146;

    Department of Civil Engineering Indian Institute of Technology Kharagpur India;

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  • 原文格式 PDF
  • 正文语种 英语
  • 中图分类 化学;
  • 关键词

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