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在移动床生物膜反应器中对刚果红染料的生物降解:性能评估和动力学建模。

Biodegradation of Congo red dye in a moving bed biofilm reactor: Performance evaluation and kinetic modeling.

机构信息

Department of Chemical Engineering & Technology, Indian Institute of Technology (BHU), Varanasi 221005, Uttar Pradesh, India.

Department of Chemical Engineering & Technology, Indian Institute of Technology (BHU), Varanasi 221005, Uttar Pradesh, India.

出版信息

Bioresour Technol. 2020 Apr;302:122811. doi: 10.1016/j.biortech.2020.122811. Epub 2020 Jan 21.

Abstract

The biodegradation of Congo red dye was performed using polyurethane foam-polypropylene immobilized Bacillus sp. MH587030.1 in a moving bed biofilm reactor (MBBR). The central composite design (CCD) based response surface methodology (RSM) was used to optimize the process parameters; pH, Congo red concentration, and media filling ratio, and optimum conditions were observed to be 7.0, 50 mg/L, and 45%, respectively in batch MBBR. At optimum condition, MBBR was operated in continuous mode at different flow rates (25-100 mL/h) over a period of 564 h. The maximum removal efficiency (RE) and elimination capacity (EC) were obtained as 95.7% and 57.6 mg/L·day, respectively under steady-state. The kinetics of Congo red biodegradation at various flow rates were evaluated by a modified Stover-Kincannon model, and kinetic constants; K and U were found to be 0.253 g/L·day and 0.263 g/L·day, respectively.

摘要

采用聚氨酯泡沫-聚丙烯固定化 Bacillus sp. MH587030.1 在移动床生物膜反应器 (MBBR) 中对刚果红染料进行生物降解。基于中心复合设计 (CCD) 的响应面法 (RSM) 用于优化工艺参数;pH 值、刚果红浓度和介质填充率,在批式 MBBR 中,分别观察到最佳条件为 7.0、50 mg/L 和 45%。在最佳条件下,MBBR 在连续模式下以不同的流速(25-100 mL/h)运行了 564 h。在稳态下,最大去除效率 (RE) 和消除容量 (EC) 分别为 95.7%和 57.6 mg/L·天。通过改进的 Stover-Kincannon 模型评估了不同流速下刚果红生物降解的动力学,发现动力学常数 K 和 U 分别为 0.253 g/L·天和 0.263 g/L·天。

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