Khelifi Eltaief, Gannoun Hana, Touhami Youssef, Bouallagui Hassib, Hamdi Moktar
Laboratory of Microbial Ecology and Technology, Department of Biological and Chemical Engineering, Institut National des Sciences Appliquées et de Technologie, 2 Boulevard de la terre, B.P. 676, 1080 Tunis, Tunisia.
J Hazard Mater. 2008 Apr 1;152(2):683-9. doi: 10.1016/j.jhazmat.2007.07.059. Epub 2007 Jul 25.
An aerobic bioprocess was applied to Indigo dye-containing textile wastewater treatment aiming at the colour elimination and biodegradation. A combined aerobic system using continuous stirred tank reactor (CSTR) and fixed film bioreactor (FFB) was continuously operated at constant temperature and fed with the textile wastewater (pH: 7.5 and total chemical oxygen demand (COD): 1185 mg l(-1)). The CSTR is a 1l continuous flow stirred tank reactor with a 700 ml working volume, and operated with a variable wastewater loading rate (WLR) from 0.92 to 3.7 g l(-1) d(-1). The FFB is a 1.5l continuous flow with three compartments packed with a rippled cylindrical polyethylene support, operated with a variable WLR between 0.09 and 0.73 g l(-1) d(-1). The combined two bioreactors were inoculated by an acclimated microbial consortium and continuously operated with four total WLR. This system presented high COD elimination and colour removal efficiencies of 97.5% and 97.3%, respectively, obtained with a total hydraulic retention time (HRT) of 4 days and total WLR of 0.29 g l(-1) d(-1). The effects of WLR on absorption phenomena on the yield of conversion of substrate on biomass (R(TSS/COD)) and on the yield of conversion of substrate on active biomass (R(VVS/COD)) are discussed. The increase of WLR and the decrease of HRT diminished the performances of this system in terms of decolourization and COD removal explained by the sloughing of biofilm, and the washout phenomena.
采用好氧生物工艺处理含靛蓝染料的纺织废水,旨在实现脱色和生物降解。使用连续搅拌釜式反应器(CSTR)和固定膜生物反应器(FFB)的组合好氧系统在恒温下连续运行,并加入纺织废水(pH值:7.5,总化学需氧量(COD):1185 mg l(-1))。CSTR是一个1升的连续流搅拌釜式反应器,工作体积为700毫升,以0.92至3.7 g l(-1) d(-1)的可变废水负荷率运行。FFB是一个1.5升的连续流反应器,有三个隔室,填充有波纹圆柱形聚乙烯载体,以0.09至0.73 g l(-1) d(-1)的可变废水负荷率运行。将两个生物反应器组合接种适应的微生物群落,并以四种总废水负荷率连续运行。该系统在总水力停留时间(HRT)为4天、总废水负荷率为0.29 g l(-1) d(-1)的情况下,分别实现了97.5%和97.3%的高COD去除率和脱色率。讨论了废水负荷率对吸收现象、底物转化为生物量的产率(R(TSS/COD))以及底物转化为活性生物量的产率(R(VVS/COD))的影响。废水负荷率的增加和水力停留时间的减少降低了该系统在脱色和COD去除方面的性能,这可以通过生物膜的脱落和冲刷现象来解释。