Ozone mass transfer in water and wastewater treatment: Experimental observations using a 2D laser particle dynamics analyzer

被引:66
作者
Zhou, HD [1 ]
Smith, DW
机构
[1] Univ Guelph, Sch Engn, Guelph, ON N1G 2W1, Canada
[2] Univ Alberta, Dept Civil & Environm Engn, Edmonton, AB T6G 2G7, Canada
关键词
ozone; ozonation; water treatment; pulp mill effluent; mass transfer; bubble size distribution; laser particle dynamics analyzer;
D O I
10.1016/S0043-1354(99)00196-7
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Ozone mass transfer in water and wastewater was studied by using a 2D laser particle dynamics analyzer (PDA) to simultaneously measure bubble size distribution and mixing intensity. Three types of water samples, including deionized water, tap water and pulp mill effluents were tested to demonstrate the enhancement of ozone absorption with the presence of chemical reactions. Bubble size distribution and apparent mass transfer rates were used to estimate individual mass transfer parameters and examine the effects of operating conditions and selected gas spargers. II was shown that gas bubbles in ozonation systems varied over a broad range of sizes and their distributions usually deviated From a simple normal distribution. Among the factors examined, the gas sparger and water types were identified as the most important factors affecting mean bubble size, whereas the impacts of ozone dose and gas flow rate on bubble size distribution were minor. Due to the higher gas holdup, however, the specific surface area was strongly dependent on the gas Row rare as well. Consequently, the mass transfer coefficient increased as the gas flow rate increased. A further enhancement of mass transfer was observed for pulp mill wastewarers as compared to tap and deionized water samples, because the occurrence of chemical reactions depleted the dissolved ozone within the gas-liquid film. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:909 / 921
页数:13
相关论文
共 18 条
[1]  
[Anonymous], 1989, STANDARD METHODS EXA, V17th
[2]  
[Anonymous], 1992, MEAS OX TRANSF CLEAN
[3]   MODELING INDUSTRIAL WASTE-WATER OZONATION IN BUBBLE CONTACTORS .1. RATE COEFFICIENT DETERMINATION [J].
BELTRAN, FJ ;
ENCINAR, JM ;
GARCIAARAYA, JF ;
MUNOZ, MG .
OZONE-SCIENCE & ENGINEERING, 1995, 17 (04) :355-378
[4]  
*CPPA, 1974, CPPA TECHN SECT H5P
[5]  
Danckwerts P.V., 1970, GAS LIQUID REACTIONS
[6]   MODELING OF AN OZONE WASTE-WATER SYSTEMS KINETICS [J].
FAROOQ, S ;
AHMED, M .
WATER RESEARCH, 1989, 23 (07) :809-815
[7]  
GRASSO D, 1989, J WPCF, V62, P246
[8]  
Langlais B., 1991, Ozone in Water Treatment: Application and Engineering
[9]   MODELING OF OZONE TRANSFER IN A BUBBLE COLUMN [J].
LESAUZE, N ;
LAPLANCHE, A ;
MARTIN, N ;
MARTIN, G .
WATER RESEARCH, 1993, 27 (06) :1071-1083
[10]  
MARINAS BJ, 1993, J AWWA, V85, P91