Effects of impurities on oxygen transfer rates in diffused aeration systems

被引:64
作者
Chern, JM [1 ]
Chou, SR [1 ]
Shang, CS [1 ]
机构
[1] Tatung Univ, Dept Chem Engn, Taipei 10451, Taiwan
关键词
mass transfer; bubble aeration; soybean oil; surfactant; suspended solids;
D O I
10.1016/S0043-1354(01)00031-8
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A series of unsteady-state reaeration tests were performed in a 500-L tank at 0.8 1-4.58 m(3)/h diffused-air flow rate and 288-302K water temperature. Three different types of impurities: soybean oil, surfactant, and diatomaceous earth were doped to simulate the impurities in wastewaters and the effects of the impurities on the oxygen transfer rate were investigated. The ASCE and the two-zone oxygen mass-transfer models were used to analyze the unsteady-state reaeration data and the volumetric mass-transfer coefficients determined from the unsteady-state reaeration data were correlated as a function of the diffused-air flow rate, water temperature, and impurity concentration. The results showed that the alpha factors based on the ASCE model are less sensitive to the impurity concentration while the presence of the impurities significantly reduces the alpha factors in the gas bubble zone. The saturation DO concentration and volumetric oxygen mass-transfer rate can be predicted by the two-zone model along with the correlation obtained in this study. (C) 2001 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:3041 / 3048
页数:8
相关论文
共 17 条
[1]  
*ASCE, 1984, ASCE STAND MEAS OX T
[2]   Alpha correction factors for static aerators and fine bubble diffusers used in municipal facultative aerated lagoons [J].
Asselin, C ;
Comeau, Y ;
Ton-That, QA .
WATER SCIENCE AND TECHNOLOGY, 1998, 38 (03) :79-85
[3]   Oxygen transfer modeling of diffused aeration systems [J].
Chern, JM ;
Yu, CF .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (12) :5447-5453
[4]   Volatile organic compound emission from diffused aeration systems: Experiment and modeling [J].
Chern, JM ;
Yu, CF .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (05) :2156-2159
[5]   VOLATILE ORGANIC-COMPOUND EMISSION RATE FROM DIFFUSED AERATION SYSTEMS .1. MASS-TRANSFER MODELING [J].
CHERN, JM ;
YU, CF .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (08) :2634-2643
[6]  
DOYLE ML, 1985, P SEM WORKSH AER SYS
[7]  
Eckenfelder W., 1989, IND WATER POLLUTION
[8]  
GILBERT RG, 1979, P WORKSH OX TRANSF S
[9]  
GUROL MD, 1985, J WATER POLLUT CON F, V57, P235
[10]   THE EFFECT OF SURFACTANT ON TERMINAL VELOCITY OF AND MASS-TRANSFER FROM A FLUID SPHERE IN A NON-NEWTONIAN FLUID [J].
KAWASE, Y ;
ULBRECHT, JJ .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1982, 60 (01) :87-93