Tokumura Masahiro, Ohta Ayano, Znad Hussein T, Kawase Yoshinori
Research Center for Biochemical and Environmental Engineering, Department of Applied Chemistry, Toyo University, Kawagoe, Saitama 350-8585, Japan.
Water Res. 2006 Dec;40(20):3775-84. doi: 10.1016/j.watres.2006.08.012. Epub 2006 Oct 9.
The photochemical decolorization of coffee effluent has been examined by photo-Fenton (UV/Fe2+/H2O2) process. Effects of UV light intensity, initial coffee concentration, iron dose and H2O2 dose on the color removal of model coffee effluent have been investigated. The rate of decolorization increased with decreasing initial coffee effluent concentration. It was found that the Fe ion dose and UV light intensity enhanced the decolorization rate. The decolorization process of coffee effluent could be divided into three established phases. At the beginning of the photo-Fenton process, the instantaneous and significant increase in color of the solution was found (Phase-I). In the subsequent phase (Phase-II), the decolorization rate was initially fast and subsequently decreased. In Phase-III, the rate was accelerated and then the complete decolorization of model coffee effluent was achieved. In order to elucidate the mechanisms of coffee effluent color removal process, the concentration changes in Fe3+ and Fe2+ besides H2O2 were measured during the course of the photo-Fenton process. The rate-determining step in Phase-II was the photo-Fenton reaction or photoreduction of Fe3+. On the other hand, the decolorization process in Phase-III was highly affected by Fenton reaction or decomposition of H2O2 with Fe2+. About 93% mineralization of 250 mg L(-1) model coffee effluent was achieved after 250 min. A comparative study for TiO2, ZnO and photo-Fenton oxidation processes has been also carried out and the photo-Fenton process was found to be the most effective for color removal of coffee effluent.
采用光芬顿(UV/Fe2+/H2O2)工艺对咖啡废水的光化学脱色进行了研究。考察了紫外光强度、初始咖啡浓度、铁剂量和过氧化氢剂量对模拟咖啡废水脱色效果的影响。脱色率随初始咖啡废水浓度的降低而增加。结果表明,铁离子剂量和紫外光强度提高了脱色率。咖啡废水的脱色过程可分为三个既定阶段。在光芬顿过程开始时,发现溶液颜色瞬间显著增加(第一阶段)。在随后的阶段(第二阶段),脱色率起初很快,随后下降。在第三阶段,速率加快,然后模拟咖啡废水实现完全脱色。为了阐明咖啡废水脱色过程的机理,在光芬顿过程中测定了除过氧化氢外Fe3+和Fe2+的浓度变化。第二阶段的速率决定步骤是光芬顿反应或Fe3+的光还原。另一方面,第三阶段的脱色过程受芬顿反应或Fe2+分解过氧化氢的影响很大。250分钟后,250mg L(-1)模拟咖啡废水的矿化率达到约93%。还对TiO2、ZnO和光芬顿氧化工艺进行了对比研究,发现光芬顿工艺对咖啡废水脱色最有效。