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Growth kinetics of an indigenous mixed microbial consortium during phenol degradation in a batch reactor

机译:间歇反应器中苯酚降解过程中原生混合微生物财团的生长动力学

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Biodegradation of phenol by a mixed microbial culture, isolated from a sewage treatment plant, was investigated in batch shake flasks. A minimum concentration of 100 and a maximum of 800 mg l(-1) of phenol in the media were adapted in the degradation study. The phenol degradation rate varied largely and was less than 10 mg l(-1) h(-1) at both extremes of the initial concentrations in the media. The degradation rate was maximum 15.7 mg l(-1) h(-1) at 400 mg l(-1) phenol. The culture followed substrate inhibition kinetics and the specific growth rate were fitted to Haldane and Han-Levenspiel models. Between the two models the Han-Levenspiel was found to be a better fit with a root mean square error of 0.0211. The biokinetics constants estimated using these models showed good potential of the mixed microbial culture in phenol degradation. (c) 2006 Elsevier Ltd. All rights reserved.
机译:在分批摇瓶中研究了从污水处理厂分离的混合微生物培养物对苯酚的生物降解作用。在降解研究中调整了培养基中最低浓度为100和最大800 mg l(-1)的苯酚。苯酚的降解速率变化很大,并且在培养基中初始浓度的两个极端值均小于10 mg l(-1)h(-1)。在400 mg l(-1)苯酚下,降解速率最大为15.7 mg l(-1)h(-1)。培养遵循底物抑制动力学,并且将比生长速率拟合至Haldane和Han-Levenspiel模型。在这两个模型之间,Han-Levenspiel被发现更适合,均方根误差为0.0211。使用这些模型估算的生物动力学常数显示出混合微生物培养物在苯酚降解中的良好潜力。 (c)2006 Elsevier Ltd.保留所有权利。

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