Wu J, Wang T
School of Chemical Engineering, Ryerson Polytechnic University, Toronto, Ontario, Canada.
Water Res. 2001 Mar;35(4):1093-9. doi: 10.1016/s0043-1354(00)00330-4.
The ozonation of wastewater containing azo dye in a semi-batch reactor has been studied. Results revealed that the rate of ozone transfer increased with increases in the initial dye concentration, the applied ozone dose and temperature. A model was developed to predict the enhancement factor of ozone mass transfer. This model enables the prediction of mass transfer coefficient of ozone from the following parameters: initial dye concentration, applied ozone dose, temperature and concentration of dissolved ozone in the organic-free water. This model was also valid for reactors of larger sizes. Result of kinetic studies showed that ozonation of the azo dye was a pseudo-first-order reaction with respect to dye. The apparent rate constant increased with the applied ozone dose and temperature. However, the apparent rate constant declined logarithmically with increasing initial dye concentration. In addition, ozonation reduced chemical oxygen demand and enhanced the biodegradability of the wastewater.
研究了在半间歇式反应器中对含偶氮染料废水进行臭氧化处理的情况。结果表明,臭氧传质速率随着初始染料浓度、臭氧投加量和温度的增加而提高。建立了一个模型来预测臭氧传质增强因子。该模型能够根据以下参数预测臭氧传质系数:初始染料浓度、臭氧投加量、温度以及无有机物水中溶解臭氧的浓度。该模型对更大尺寸的反应器也有效。动力学研究结果表明,偶氮染料的臭氧化反应对染料而言是准一级反应。表观速率常数随臭氧投加量和温度的增加而增大。然而,表观速率常数随着初始染料浓度的增加呈对数下降。此外,臭氧化处理降低了化学需氧量并提高了废水的生物降解性。