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采用厌氧批式反应器处理纺织染料废水的生物动力学分析。

Bio-kinetic analysis on treatment of textile dye wastewater using anaerobic batch reactor.

机构信息

Department of Civil Engineering, Annamalai University, Annamalainagar 608 002, India.

出版信息

Bioresour Technol. 2011 Jan;102(2):627-32. doi: 10.1016/j.biortech.2010.08.012. Epub 2010 Aug 6.

Abstract

An anaerobic digestion technique was applied to textile dye wastewater aiming at the colour and COD removal. Pet bottles of 5 L capacity were used as reactor which contains methanogenic sludge of half a liter capacity which was used for the treatment of combined synthetic textile dye and starch wastewater at different mixing ratios of 20:80, 30:70, 40:60, 50:50 and 60:40 with initial COD concentrations as 3520, 3440, 3360, 3264 and 3144 mg L(-1), respectively. The reactor was maintained at room temperature (30±3°C) with initial pH of 7. The maximum COD and colour removal were 81.0% and 87.3% at an optimum mixing ratio of 30:70 of textile dye and starch wastewaters. Both Monod's and Haldane's models were adopted in this study. The kinetic constants of cell growth under Haldane's model were satisfactory when compared to Monod's model. The kinetic constants obtained by Haldane's model were found to be in the range of μmax=0.037-0.146 h(-1), Ks=651.04-1372.88 mg L(-1) and Ki=5681.81-18727.59 mg L(-1).

摘要

采用厌氧消化技术处理纺织染料废水,以去除颜色和 COD。使用 5 升容量的 PET 瓶作为反应器,其中含有半升甲烷菌污泥,用于处理不同混合比例的组合合成纺织染料和淀粉废水,混合比例分别为 20:80、30:70、40:60、50:50 和 60:40,初始 COD 浓度分别为 3520、3440、3360、3264 和 3144 mg/L。反应器保持在室温(30±3°C),初始 pH 值为 7。在纺织染料和淀粉废水的最佳混合比例为 30:70 时,最大 COD 和颜色去除率分别为 81.0%和 87.3%。本研究采用了 Monod 模型和 Haldane 模型。与 Monod 模型相比,Haldane 模型下细胞生长的动力学常数更令人满意。通过 Haldane 模型获得的动力学常数范围为 μmax=0.037-0.146 h(-1)、Ks=651.04-1372.88 mg/L 和 Ki=5681.81-18727.59 mg/L。

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