首页> 外文期刊>Applied Microbiology and Biotechnology >Benzene/toluene/p-xylene degradation. Part II. Effect of substrate interactions and feeding strategies in toluene/benzene and toluene/p-xylene fermentations in a partitioning bioreator
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Benzene/toluene/p-xylene degradation. Part II. Effect of substrate interactions and feeding strategies in toluene/benzene and toluene/p-xylene fermentations in a partitioning bioreator

机译:苯/甲苯/对二甲苯降解。第二部分分配生物反应器中甲苯/苯和甲苯/对二甲苯发酵中底物相互作用和进料策略的影响

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A two-phase aqueous/organic partitioning bioreactor scheme was used to degrade mixtures of toluene and benzene, and toluene and p-xylene, using simultaneous and sequential feeding strategies. The aqueous phase of the partitioning bioreactor contained Pseudomonas sp. ATCC 55595, an organism able to degrade benzene, toluene and p-xylene simultaneously. An industrial grade of oleyl alcohol served as the organic phase. In each experiment, the organic phase of the bioreactor was loaded with 10.15 g toluene, and either 2.0 g benzene or 2.1 g p-xylene. The resulting aqueous phase concentrations were 50 mg/l, 25 mg/l and 8 mg/l toluene, benzene and p-xylene respectively. The simultaneous fermentation of benzene and toluene consumed these compounds at volumetric rates of 0.024 g l~(-1) h~(-1) and 0.067 g l~(-1) h~(-1), respectively. The simultaneous fermentation of toluene and p-xylene consumed these xenobiotics at volumetric rates of 0.066 g l~(-1) h~(-1) and 0.018 g l~(-1) h~(-1), respectively. A sequential feeding strategy was employed in which toluene was added initially, but the benzene or p-xylene aliquot was added only after the cells had consumed half of the initial toluene concentration. This strategy was shown to improve overall degradation rates, and to reduce the stress on the microorganisms. In the sequential fermentation of benzene and toluene, the volumetric degradation rates were 0.056 g l~(-1) h~(-1) and 0.079 g l~(-1) h~(-1), respectively. In the toluene/p-xylene sequential fermentation, the initial toluene load was consumed before the p-xylene aliquot was consumed. After 12 h in which no p-xylene degradation was observed, a 4.0-g toluene aliquot was added, and p-xylene degradation resumed. Excluding that 12-h period, the microbes consumed toluene and p-xylene at volumetric rates of 0.074 g l~(-1) h~(-1) and 0.025 g l~(-1) h~(-1), respectively. Oxygen limitation occurred in all fermentations during the rapid growth phase.
机译:使用两相水/有机分配生物反应器方案,使用同时和顺序进料策略,降解甲苯和苯以及甲苯和对二甲苯的混合物。分配生物反应器的水相包含假单胞菌sp。 ATCC 55595,一种能够同时降解苯,甲苯和对二甲苯的生物。工业级油醇用作有机相。在每个实验中,生物反应器的有机相均装有10.15克甲苯和2.0克苯或2.1克对二甲苯。所得水相浓度分别为50mg / l,25mg / l和8mg / l的甲苯,苯和对二甲苯。苯和甲苯的同时发酵分别消耗了0.024 g l〜(-1)h〜(-1)和0.067 g l〜(-1)h〜(-1)的这些化合物。甲苯和对二甲苯的同时发酵消耗了这些异生物素,其体积比分别为0.066 g l〜(-1)h〜(-1)和0.018 g l〜(-1)h〜(-1)。采用了顺序进料策略,其中先加入甲苯,但仅在电池消耗了初始甲苯浓度的一半后才加入苯或对二甲苯等分试样。该策略显示出可以提高整体降解率,并减少对微生物的压力。在苯和甲苯的顺序发酵中,体积降解速率分别为0.056 g l〜(-1)h〜(-1)和0.079 g l〜(-1)h〜(-1)。在甲苯/对二甲苯连续发酵中,在消耗对二甲苯等分试样之前先消耗了初始甲苯负载量。在没有观察到对二甲苯降解的12小时之后,加入4.0g甲苯等分试样,并且对二甲苯恢复降解。除12 h时段外,微生物分别以0.074 g l〜(-1)h〜(-1)和0.025 g l〜(-1)h〜(-1)的体积消耗甲苯和对二甲苯。在快速生长阶段的所有发酵过程中都发生了氧气限制。

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