首页> 外文期刊>Chemosphere >Photocatalytic degradation of humic acid in saline waters. Part 1. Artificial seawater: influence of TiO2, temperature, pH, and air-flow
【24h】

Photocatalytic degradation of humic acid in saline waters. Part 1. Artificial seawater: influence of TiO2, temperature, pH, and air-flow

机译:盐水中腐殖酸的光催化降解。第1部分:人造海水:TiO2,温度,pH和气流的影响

获取原文
获取原文并翻译 | 示例
获取外文期刊封面目录资料

摘要

We report the first systematic study on the photocatalytic oxidation of humic acid (HA) in artificial seawater (ASW). TiO2 (Degussa P25) dispersions were used as the catalyst with irradiation from a medium-pressure mercury lamp. The optimum quantity of catalyst was found to be between 2 and 2.5 g l(-1); whiled the decomposition was fastest at low pH values (pH 4.5 in the range examined), and the optimum air-flow, using an immersion well reactor with a capacity of 400 ml, was 850 ml min(-1). Reactivity increased with air-flow up to this figure, above which foaming prevented operation of the reactor. Using pure. oxygen, an optimal flow rate was observed at 300 nil min(-1), above which reactivity remains essentially constant. Following treatment for 1 h, low-salinity water (2700 mg l(-1)) was completely mineralised, whereas ASW (46000 mg l(-1)) had traces of HA remaining. These effects are interpreted and kinetic data presented. To avoid problems of precipitation due to change of ionic strength humic substances were prepared directly in ASW, and the effects of ASW on catalyst suspension and precipitation have been taken into account. The Langmuir-Hinshelwood kinetic model has been shown to be followed only approximately for the catalytic oxidation of HA in ASW. The activation energy for the reaction derived from an Arrhenius treatment was 17 ( +/-0.6) kJ mol(-1). (C) 2003 Elsevier Science Ltd. All rights reserved. [References: 35]
机译:我们报告了对人工海水(ASW)中的腐殖酸(HA)光催化氧化的第一个系统研究。在中压汞灯照射下,将TiO2(Degussa P25)分散液用作催化剂。发现催化剂的最佳量为2到2.5 g l(-1)。而在低pH值(在所检查范围内的pH值为4.5)下,分解最快,而使用容量为400 ml的浸入式孔反应器的最佳气流为850 ml min(-1)。直到该数字,反应性随气流增加而增加,在此之上起泡阻止反应器运行。使用纯。氧气,在300 nil min(-1)处观察到最佳流速,在此之上反应性基本保持恒定。处理1小时后,低盐度水(2700 mg l(-1))完全矿化,而ASW(46000 mg l(-1))则残留有HA。解释这些作用并提供动力学数据。为避免由于离子强度变化而引起的沉淀问题,直接在ASW中制备了腐殖质,并考虑了ASW对催化剂悬浮和沉淀的影响。 Langmuir-Hinshelwood动力学模型仅在ASW中催化HA的氧化反应中得到遵循。来自Arrhenius处理的反应的活化能为17(+/- 0.6)kJ mol(-1)。 (C)2003 Elsevier ScienceLtd。保留所有权利。 [参考:35]

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号