Characterization of micro-bubble size distribution and flow configuration in DAF contact zone by a non-intrusive image analysis system and tracer tests

被引:31
作者
Moruzzi, R. B. [1 ]
Reali, M. A. P. [2 ]
机构
[1] Paulista State Univ UNESP, Geoproc & Terr Planning Dept DEPLAN, Geosci & Math Inst IGCE, BR-13500230 Rio Claro, SP, Brazil
[2] Univ Sao Paulo EESC USP, Sao Carlos Sch Engn, Dept Hydraul & Sanitat, BR-13566590 Sao Carlos, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
bubbles sizes; contact zone; DAF; image analysis; DISSOLVED AIR FLOTATION; WATER-TREATMENT; PARTICLE-SIZE; EFFICIENCY; ATTACHMENT; COLLISION;
D O I
10.2166/wst.2010.784
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This paper aims to investigate the influence of some dissolved air flotation (DAF) process variables (specifically: the hydraulic detention time in the contact zone and the supplied dissolved air concentration) and the pH values, as pretreatment chemical variables, on the micro-bubble size distribution (BSD) in a DAF contact zone. This work was carried out in a pilot plant where bubbles were measured by an appropriate non-intrusive image acquisition system. The results show that the obtained diameter ranges were in agreement with values reported in the literature (10-100mm), quite independently of the investigated conditions. The linear average diameter varied from 20 to 30mm, or equivalently, the Sauter (d(3,2)) diameter varied from 40 to 50mm. In all investigated conditions, D(50) was between 75% and 95%. The BSD might present different profile (with a bimodal curve trend), however, when analyzing the volumetric frequency distribution (in some cases with the appearance of peaks in diameters ranging from 90-100mm). Regarding volumetric frequency analysis, all the investigated parameters can modify the BSD in DAF contact zone after the release point, thus potentially causing changes in DAF kinetics. This finding prompts further research in order to verify the effect of these BSD changes on solid particle removal efficiency by DAF.
引用
收藏
页码:253 / 262
页数:10
相关论文
共 28 条
[1]   The formation of bubble clusters in flotation cells [J].
Ata, S ;
Jameson, GJ .
INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 2005, 76 (1-2) :123-139
[2]   Development and application of an image analysis method for wide bubble size distributions [J].
Bailey, M ;
Gomez, CO ;
Finch, JA .
MINERALS ENGINEERING, 2005, 18 (12) :1214-1221
[3]   EFFECTS OF BUBBLE SIZE ON MICROFLOTATION [J].
CASSELL, EA ;
KAUFMAN, KM ;
MATIJEVIC, E .
WATER RESEARCH, 1975, 9 (12) :1017-1024
[4]   PRINCIPLES AND APPLICATIONS OF DISSOLVED AIR FLOTATION [J].
EDZWALD, JK .
WATER SCIENCE AND TECHNOLOGY, 1995, 31 (3-4) :1-23
[5]   COLLISION EFFICIENCY OF SMALL PARTICLES WITH SPHERICAL AIR BUBBLES [J].
FLINT, LR ;
HOWARTH, WJ .
CHEMICAL ENGINEERING SCIENCE, 1971, 26 (08) :1155-&
[6]   A KINETIC-MODEL FOR DISSOLVED AIR FLOTATION IN WATER AND WASTE-WATER TREATMENT [J].
FUKUSHI, K ;
TAMBO, N ;
MATSUI, Y .
WATER SCIENCE AND TECHNOLOGY, 1995, 31 (3-4) :37-47
[7]   Bubble load estimation in the froth zone to predict the concentrate mass flow rate of solids in column flotation [J].
Gallegos-Acevedo, P. M. ;
Perez-Garibay, R. ;
Uribe-Salas, A. ;
Nava-Alonso, F. .
MINERALS ENGINEERING, 2007, 20 (13) :1210-1217
[8]   Modelling of floc-bubble aggregate rise rates in dissolved air flotation [J].
Haarhoff, J ;
Edzwald, JK .
WATER SCIENCE AND TECHNOLOGY, 2001, 43 (08) :175-184
[9]   Dissolved air flotation modelling: insights and shortcomings [J].
Haarhoff, J ;
Edzwald, JK .
JOURNAL OF WATER SUPPLY RESEARCH AND TECHNOLOGY-AQUA, 2004, 53 (03) :127-150
[10]   Development of a new method of measuring bubble size [J].
Han, MY ;
Park, YH ;
Yu, TJ .
2ND WORLD WATER CONGRESS: DRINKING WATER TREATMENT, 2002, 2 (02) :77-83