Quantitative characterization of organic diffusion using an analytical diffusion-reaction model and its application to assessing BOD removal when treating municipal wastewater in a plug flow reactor

被引:7
作者
Fan, Chihhao [1 ]
Kao, Chen-Fei [2 ]
Liu, Yu-Hsi [1 ]
机构
[1] Natl Taiwan Univ, Dept Bioenvironm Syst Engn, 1,Sec 4,Roosevelt Rd, Taipei 106, Taiwan
[2] Formosa Chem & Fiber Corp, 359,Sec 3,Zhongshan Rd, Changhua 500, Changhua County, Taiwan
关键词
Wastewater treatment; Biofilm; Diffusion coefficient; Biochemical oxygen demand; Domestic sewage; BIOFILM THICKNESS; SIMULATION; FILTER; COEFFICIENTS; SYSTEM; OXYGEN;
D O I
10.1016/j.watres.2017.05.050
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The present study aimed to derive an analytical formula to quantify the diffusion of organic contaminant in a biofilm. The experiments were conducted to investigate the BOD degradation under the conditions of influent COD concentration from 50 to 300 mg/L, COD:N:P ratios of 100:5:1 and 100:15:3, with and without auxiliary aeration. The BOD removal rate was around 73% for non-aerated influent COD of 50 mg/L with 1-h hydraulic retention time. The BOD removal rate increased as the influent loading and hydraulic retention time increased while the influent COD was no more than 150 mg/L. Without aeration, the removal rate dropped significantly when influent COD increased to the range no less than 200 mg/L, due to the fact that the BOD diffusive flux driven by the biomass uptake was not further enhanced by higher ambient organic loading. The diffusion coefficient was calculated to be 1.12 x 10(-6) m(2)/d with influent COD of 50 mg/L at COD:N:P ratio of 100:5:1 and 1 h hydraulic retention time and aeration, and the coefficient increased to 3.35 x 10(-6) m(2)/d as the influent COD concentration increased to 300 mg/L. The diffusion coefficient decreased to 4.09 x 10(-7) m(2)/d as the retention time increased to 3 h. The overall diffusion coefficients showed an increasing trend as the influent organic loading increased. The difference in diffusion coefficients between 1 and 2 h was apparently greater than that between 2 and 3 h, indicating a smaller overall diffusive flux due to a longer retention time. Further analysis revealed that BOD diffusion activity exhibited a declining trend as the wastewater travelled through the system. An analytical diffusion-reaction model was developed to characterize the diffusion behaviour, and applied to estimating the treatment efficiency for real domestic sewage. The result showed that the estimated effluent BOD concentrations were quite comparable to those from experimental measurements. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:329 / 337
页数:9
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