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Heat Treatment Effect of Zinc Oxide on the Sonocatalytic Degradation of Organic Dyes

机译:氧化锌对有机染料松催化降解的热处理效果

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Sonocatalytic degradation of Methyl Orange in a 40 kHz, 124 W ultrasonic bath was carried out in the presence of zinc oxide (ZnO) catalyst. The catalysts were subjected to heat treatment from 200 °C to 800 °C for 2 hours and were characterised by X-ray diffraction (XRD) and scanning electron microscopy (SEM) analyses. XRD confirmed that no phase change occurred even though calcined up to 800 °C whereas SEM showed that catalysts started to undergo aggregation when the heat treatment temperature was raised to 600 °C. The effect of initial dye concentration, catalyst loading, pH and hydrogen peroxide (H_2O_2) concentration on the sonocatalytic activity were carried out at 2.5 mg/L to 12.5 mg/L, 0.2 g/L to 1.0 g/L, pH 2 to pH 10 and 0.5 to 2.5 mmol/L, respectively. The optimum operating conditions discovered were 2.5 mg/L initial dye concentration, 0.8 g/L catalyst loading, pH 6 solution and 1.0 mmol/L H_2O_2 concentration, which successfully removed 71.42 % of Methyl Orange in 1 hour. The sonocatalytic degradation efficiency of the reused catalyst were 64.4 % and 59.6 % in the subsequent usage.
机译:在40kHz的甲基橙的催化超声降解,124W¯¯超声浴中在氧化锌(ZnO)的催化剂的存在下进行。该催化剂进行热处理从200℃至800℃下进行2小时,并用X射线衍射(XRD)和扫描电子显微镜(SEM)分析。 XRD证实,无相变发生,即使煅烧高达800℃,而SEM表明开始当热处理温度升高到600℃经历聚集是催化剂。初始染料浓度,催化剂负载,pH值和在声催化活性过氧化氢(H_2O_2)浓度的影响进行了以2.5mg / L进行到12.5毫克/升,0.2克/升至1.0g / L,pH为2至pH 10和0.5〜2.5毫摩尔/ L,分别。发现的最佳操作条件分别为2.5毫克/升的初始染料浓度,0.8 g / L的催化剂负载量,pH为6溶液和1.0毫摩尔/ L H_2O_2浓度,其在1小时内成功移除甲基橙的71.42%。重用催化剂的声催化降解效率分别为64.4%,并在后续使用59.6%。

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