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Treatment of anthranilic acid in an anaerobic expanded granular sludge bed reactor at low concentrations

机译:低浓度厌氧膨胀颗粒污泥床反应器中邻氨基苯甲酸的处理

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The mineralization of anthranilic acid (2AB) as the only carbon and energy source was studied in batch and continuous conditions using methanogenic granular slude. Under batch conditions in serum vials, 2AB (300 mg/l) was completely mineralized to methane within 55 days time. The experiment with the anaerobic continuous expanded granular sludge bed (EGSB) reactor was initially conducted at an upflow velocity (V_(up))of 5 m/h, a hydraulic retention time (HRT) of 12 h and an organic loading rate (OLR) of 1.5 g chemical oxygen demand (COD)/1-d. After 102 days, 2AB was not degraded at all and the reactor operation was shifted to batch mode by recycling the effluent. After some days, 2AB was completely mineralized and accumulation of flocculent sludge was observed. Batch biodegradability assays demonstrated that this flocculent biomass had a higher specific biodegradation rate compared to the granular sludge. During EGSB reactor operation, the flocculent biomass which was not attached to the granulet probably washed-out under the applied hydrodynamic conditions. When the EGSB reactor was operated at V_(up) of 2 m/h to favour the retention of the flocculent biomass, 2AB was mineralized even at influent concentrations as low as 140 mg COD/L. Kinetic calculations indicated that the sludge had an apparent K_s value for the mineralization of 2AB as low as 24 mg COD/l.
机译:使用产甲烷颗粒污泥在间歇和连续条件下研究了邻氨基苯甲酸(2AB)作为唯一碳和能源的矿化作用。在血清瓶中分批处理的条件下,在55天之内将2AB(300 mg / l)完全矿化为甲烷。厌氧连续膨胀颗粒污泥床(EGSB)反应器的实验最初是在5 m / h的上升速度(V_(up)),12 h的水力停留时间(HRT)和有机负荷率(OLR)下进行的1.5克化学需氧量(COD)/ 1-d。 102天后,2AB完全不降解,并且通过回收流出物将反应器操作转换为间歇模式。几天后,2AB完全矿化,并观察到了絮状污泥的积累。分批生物降解性试验表明,与颗粒污泥相比,该絮凝生物质具有更高的比生物降解率。在EGSB反应器运行期间,未附着在颗粒上的絮凝生物质在所施加的流体动力学条件下可能会被洗掉。当EGSB反应器在V_up 2 m / h下运行以促进絮凝生物质的保留时,即使进水浓度低至140 mg COD / L,2AB也会矿化。动力学计算表明,对于2AB矿化,污泥的表观K_s值低至24 mg COD / l。

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