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Kinetics of municipal sewage degradation in EGSB and UASB reactors at 10℃

机译:EGSB和UASB反应器中10℃下城市污水降解的动力学

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Kinetics of municipal sewage degradation in Expanded Granular Sludge Bed (EGSB) and Up-flow Anaerobic Sludge Blanket (UASB) reactors at 10℃ were investigated via continuous experimental equipments. The results indicated that the whole reaction process can be simulated by the first-order dynamic equation model. Dynamic parameters such as k, Vmax and Ks of UASB in hydrolysis acidification stage were 1. 08 d~(-1), 2. 8 d~(-1) and 372 mg/L comparing to those of 1.18 d~(-1), 3. 5 d~(-1) and 112 mg/L in the methanogenesis stage respectively. The EGSB's k, Vmax and Ks were 2. 91 d~(-1), 14. 3 d~(-1) and 470 mg/L in the hydrolysis acidification stage comparing to those of 1. 68 d~(-1), 6. 6 d~(-1) and 103 mg/L in the methanogenesis stage respectively. Comparison of k values of the two stages in UASB and EGSB indicates that hydrolysis acidification stage is the controlling step for the whole reaction process of UASB, while methanogenesis stage is the controlling step in EGSB. Compared with UASB, municipal sewage treatment by EGSB at 10℃ can reach the same effluent requirement with lower retention time due to its effluent recirculation.
机译:通过连续实验设备研究了膨胀颗粒污泥床(EGSB)和上流厌氧污泥毯(UASB)反应器在10℃下城市污水降解的动力学。结果表明,整个反应过程可以通过一阶动力学方程模型进行模拟。水解酸化阶段UASB的k,Vmax和Ks等动力学参数分别为1.18 d〜(-1),1。08 d〜(-1),2。8 d〜(-1)和372 mg / L。 ),3。5 d〜(-1)和112 mg / L在甲烷生成阶段。水解酸化阶段的EGSB的k,Vmax和Ks分别为2. 91 d〜(-1),14。3 d〜(-1)和470 mg / L,而1.68 d〜(-1)产甲烷阶段分别为6. 6 d〜(-1)和103 mg / L。比较UASB和EGSB中两个阶段的k值,表明水解酸化阶段是UASB整个反应过程的控制步骤,甲烷化阶段是EGSB的控制步骤。与UASB相比,由于EGSB的废水再循环,在10℃下通过EGSB处理城市污水可以达到相同的废水要求,并且保留时间更短。

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