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Kinetic development and evaluation of membrane sequencing batch reactor (MSBR) with mixed cultures photosynthetic bacteria for dairy wastewater treatment

机译:混合培养光合细菌膜测序间歇反应器(MSBR)动力学开发和评价

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This experimental study was conducted to evaluate a membrane sequencing batch reactor (MSBR) with mixed culture photosynthetic bacteria for dairy wastewater treatment. The study was undertaken in two steps: laboratory and pilot scale experiments. In the first step, kinetics analysis of the MSBR was carried out in a laboratory scale experiment with influent COD concentration of 2500 mg/L The pilot scale experiment was conducted to investigate the performance of the MSBR and checked the suitability of the kinetics for an engineering design. The kinetic coefficients K_s, k, k_d, Y and μm were found to be 174-mg-COD/L, 7.42/d, 0.1383/d, 0.2281/d and 1.69/d, respectively. There were some deviations of COD removal efficiency between the design value and the actual value. From the kinetics estimation, COD effluent from the design was 27 mg/ L while the average actual COD effluent from the experiment was 149 mg/L. Due to the different light source condition, the factors relating to light energy (i.e. L-f and IR%) must be incorporated into engineering design and performance prediction with these kinetic coefficients of the photosynthetic MSBR.
机译:进行该实验研究以评估具有混合培养光合细菌的膜测序间歇反应器(MSBR),用于乳品废水处理。该研究分两个步骤进行:实验室和中试规模的实验。第一步,在实验室规模的实验中对MSBR进行动力学分析,进水COD浓度为2500 mg / L。进行了中试规模的实验,以研究MSBR的性能并检查动力学在工程上的适用性。设计。发现动力学系数K_s,k,k_d,Y和μm分别为174-mg-COD / L,7.42 / d,0.1383 / d,0.2281 / d和1.69 / d。在设计值和实际值之间有一些COD去除效率的偏差。根据动力学估算,设计中的COD排放量为27 mg / L,而实验中的平均实际COD排放量为149 mg / L。由于光源条件不同,必须使用光合MSBR的这些动力学系数将与光能有关的因素(即L-f和IR%)纳入工程设计和性能预测中。

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