Investigation of induction of air due to ultrasound source in the sonochemical reactors

被引:21
作者
Kumar, A
Gogate, PR
Pandit, AB [1 ]
Wilhelm, AM
Delmas, H
机构
[1] MUICT, Div Chem Engn, Bombay 400019, Maharashtra, India
[2] UMR 5503, Lab Genie Chim, F-31106 Toulouse, France
关键词
sonochemical reactors; air entrainment; volumetric mass transfer coefficient; ultrasonic horn; dynamic method; salt enhancement; surfactant;
D O I
10.1016/j.ultsonch.2004.05.016
中图分类号
O42 [声学];
学科分类号
070206 ; 082403 ;
摘要
A detailed investigation into the phenomena of induction of air using a novel arrangement of the ultrasonic horn (tip is located just above the liquid surface) has been made with the quantification of the extent of induction in terms of the air entrainment rate and the gas-liquid mass transfer coefficient for the transfer of air into the system. The measurement of air entrainment rate was found to be quite difficult and hence focus was kept on the quantification in terms of the gas-liquid mass transfer coefficient. The effect of ultrasonic power dissipation and type of the liquid medium (water, sodium chloride and sodium laruyl sulphate [surfactant] solution) on the mass transfer coefficient has been studied and correlations have been developed for the prediction of the same. Comparison with the mechanically agitated surface aerators has enabled us to understand the controlling mechanism in the induction and subsequent distribution of the air i.e. turbulence or convective motion. The present work should open an entirely new field of research in the area of design of sonochemical gas-liquid reactors operating possibly as a combination of gas-inducing reactors and cavitational reactors. (c) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:453 / 460
页数:8
相关论文
共 15 条
[1]   MASS-TRANSFER IN MULTIPHASE AGITATED CONTACTORS [J].
ALBAL, RS ;
SHAH, YT ;
SCHUMPE, A ;
CARR, NL .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1983, 27 (02) :61-80
[2]   Survey of measurement techniques for gas-liquid mass transfer coefficient in bioreactors [J].
Gogate, PR ;
Pandit, AB .
BIOCHEMICAL ENGINEERING JOURNAL, 1999, 4 (01) :7-15
[3]   Cavitation reactors: Efficiency assessment using a model reaction [J].
Gogate, PR ;
Shirgaonkar, IZ ;
Sivakumar, M ;
Senthilkumar, P ;
Vichare, NP ;
Pandit, AB .
AICHE JOURNAL, 2001, 47 (11) :2526-2538
[4]   Degassing effect and gas-liquid transfer in a high frequency sonochemical reactor [J].
Gondrexon, N ;
Renaudin, V ;
Boldo, P ;
Gonthier, Y ;
Bernis, A ;
Petrier, C .
CHEMICAL ENGINEERING JOURNAL, 1997, 66 (01) :21-26
[5]   Gas-liquid mass transfer studies in sonochemical reactors [J].
Kumar, A ;
Gogate, PR ;
Pandit, AB ;
Delmas, H ;
Wilhelm, AM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (08) :1812-1819
[6]   High bubble concentrations produced by ultrasounds in binary mixtures [J].
Louisnard, O ;
Lyczko, N ;
Espitalier, F ;
Urzedowski, M ;
Vargas-Hernandez, Y ;
Sanchez-Romero, C .
ULTRASONICS SONOCHEMISTRY, 2001, 8 (03) :183-189
[7]  
LUCHE JL, 1999, SYNTHETIC ORGANIC CH
[8]  
MATSUMURA M, 1979, J FERMENT TECHNOL, V57, P107
[9]  
MIKKOLA JP, 2002, PROC INN PROC INT C
[10]   The role of convection and turbulent dispersion in blending [J].
Patwardhan, AW ;
Pandit, AB ;
Joshi, JB .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (13) :2951-2962