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Removal of aqueous benzene in the immobilized batch and continuous packed bed bioreactor by isolated Bacillus sp. M1

机译:通过分离的芽孢杆菌属菌种去除固定的批次和连续填充床生物反应器中的苯水溶液。 M1

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Benzene biodegradation was studied in batch and continuous packed bed bioreactors using polyurethane foam (PUF) as packing media by isolated Bacillus sp. M1. The values of optimized process parameters were found to be 800?×?106?CFU?mL?1, 400?mg?L?1, 7.0 and 37?°C for inoculum size, substrate concentration, pH and temperature respectively. Continuous packed bed bioreactor (CPBBR) was operated and monitored for 69 days on laboratory scale at various flow rates (10–60?mL?h?1). The steady state removal efficiency was observed more than 90% up to the inlet load of 288?mg?L?1.d?1 and elimination capacity was found to be 91.2–266.4?mg?L?1?day?1. Monod growth model was applied for the removal of benzene and values were found to be (Ks: 215.07?mg?L?1; μmax: 0.314 day?1).
机译:使用分离的芽孢杆菌属(Bacillus sp。),以聚氨酯泡沫(PUF)为填充介质,研究了分批和连续填充床生物反应器中苯的生物降解。 M1。发现优化的工艺参数值为800?×?10 6? CFU?mL ?1 ,400?mg?L ?1 分别为7.0和37°C,分别用于接种物大小,底物浓度,pH和温度。连续填充床生物反应器(CPBBR)在各种流量(10–60?mL?h ?1 )下在实验室规模下运行和监测69天。直到入口负荷为288?mg?L ?1 .d ?1 为止,稳态去除效率均超过90%,消除能力为91.2 –266.4?mg?L ?1 ?day ?1 。应用Monod生长模型去除苯,其值为(K s :215.07?mg?L ?1 max >:0.314天?1 )。

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