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恶臭假单胞菌F1培养物对悬浮生长生物反应器中甲苯负荷波动和操作故障的响应。

Response of Pseudomonas putida F1 cultures to fluctuating toluene loads and operational failures in suspended growth bioreactors.

作者信息

Muñoz Raúl, Díaz Luís Felipe, Bordel Sergio, Villaverde Santiago

机构信息

Department of Chemical Engineering and Environmental Technology, University of Valladolid, Paseo del Prado de la Magdalena s/n, Valladolid, Spain.

出版信息

Biodegradation. 2008 Nov;19(6):897-908. doi: 10.1007/s10532-008-9191-5. Epub 2008 Apr 12.

Abstract

The response of Pseudomonas putida F1 to process fluctuations and operational failures during toluene biodegradation was evaluated in a chemostat suspended growth bioreactor. The ability of P. putida F1 to rapidly increase its specific toluene degradation capacity resulted in no significant variation in process removal efficiency when toluene load was increased from 188 to 341 g m(-3) h(-1). Likewise, bacterial activity rapidly reached steady state performance (in less than 1.5 h after the restoration of steady state operational conditions) following an 8 h process shutdown, or after episodes of toluene or mineral nutrients deprivation. Process performance was however highly sensitive to pH, as pH levels below 4.5 dramatically inhibited bacterial activity, decreasing severely process robustness and inducing a cycle of periodic process collapses and recoveries. This pH mediated deterioration of bacterial activity was confirmed by further respirometric tests, which revealed a 50-60% reduction in the O(2) consumption rate during the degradation of both toluene and 3-methyl catechol when pH decreased from 5.05 to 4.55. Finally, process robustness was quantified according to methods previously described in literature.

摘要

在恒化器悬浮生长生物反应器中评估了恶臭假单胞菌F1在甲苯生物降解过程中对工艺波动和操作故障的响应。当甲苯负荷从188增加到341 g m(-3) h(-1)时,恶臭假单胞菌F1迅速提高其特定甲苯降解能力的能力导致工艺去除效率没有显著变化。同样,在8小时的工艺停机后,或在甲苯或矿物质营养物质剥夺事件后,细菌活性在恢复稳态操作条件后不到1.5小时内迅速达到稳态性能。然而,工艺性能对pH值高度敏感,因为pH值低于4.5会显著抑制细菌活性,严重降低工艺稳健性,并引发周期性工艺崩溃和恢复的循环。进一步的呼吸测定试验证实了这种pH介导的细菌活性恶化,该试验表明,当pH值从5.05降至4.55时,甲苯和3-甲基邻苯二酚降解过程中的氧气消耗率降低了50-60%。最后,根据文献中先前描述的方法对工艺稳健性进行了量化。

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