Mapping of sonochemical reactors: Review, analysis, and experimental verification

被引:180
作者
Gogate, PR [1 ]
Tatake, PA [1 ]
Kanthale, PM [1 ]
Pandit, AB [1 ]
机构
[1] Univ Bombay, Inst Chem Technol, Div Chem Engn, Bombay 400019, Maharashtra, India
关键词
D O I
10.1002/aic.690480717
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The erratic behavior of cavitational activity, exhibited in a sonochemical reactor poses a serious problem in its design and scale-up. Several previous studies in the past dealt with mapping of sonochemical reactors, which have been critically analyzed and recommended for efficient scale-up strategies. There have been no efforts to link the primary effects (local pressure field) of ultrasound activity with the observed secondary effects (such as chemical reaction). In this work an ultrasonic horn (standard immersion-type reactor), and an ultrasonic bath (rectangular geometry with transducers located at the bottom in triangular pitch) reactors were mapped with the help of local pressure measurement (using a hydrophone), and liberated iodine was estimated using the Weissler reaction, and a quantitative relationship was established between the two. In estimating chemical reaction rates, the effect of microscopic variation in the type of microreactor used (test tube in this case) on the extent of degradation was also investigated. Measured local pressure pulses were used in theoretical simulations of bubble dynamics equations to check the type of cavitation taking place locally, and to estimate the possible collapse of the pressure pulse in terms of the maximum bubble size reached during the cavitation phenomena. A relationship also was established between observed iodine liberation rates and the maximum bubble size reached. The engineers can easily use these unique relationships in an efficient design, since the secondary effect can be directly quantified.
引用
收藏
页码:1542 / 1560
页数:19
相关论文
共 100 条
[1]  
AMBULGEKAR PV, 2002, IN PRESS CHEM ENG
[2]  
[Anonymous], 1952, ACTA ACUST UNITED AC
[3]   SONOCHEMICAL DESTRUCTION OF CHLORINATED-C1 AND CHLORINATED-C2 VOLATILE ORGANIC-COMPOUNDS IN DILUTE AQUEOUS-SOLUTION [J].
BHATNAGAR, A ;
CHEUNG, HM .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1994, 28 (08) :1481-1486
[4]   SONOCHEMICAL DESTRUCTION OF CHLORINATED HYDROCARBONS IN DILUTE AQUEOUS-SOLUTION [J].
CHEUNG, HM ;
BHATNAGAR, A ;
JANSEN, G .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1991, 25 (08) :1510-1512
[5]   QUANTIFICATION OF CAVITATION INTENSITY IN FLUID BULK [J].
CHIVATE, MM ;
PANDIT, AB .
ULTRASONICS SONOCHEMISTRY, 1995, 2 (01) :S19-S25
[6]   Chemical bubble dynamics and quantitative sonochemistry [J].
Colussi, AJ ;
Weavers, LK ;
Hoffmann, MR .
JOURNAL OF PHYSICAL CHEMISTRY A, 1998, 102 (35) :6927-6934
[7]   Chemical reactions under ultrasound: Discrimination of chemical and physical effects [J].
Contamine, F. ;
Faid, F. ;
Wilhelm, A. M. ;
Berlan, J. ;
Delmas, H. .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (24B) :5865-5873
[8]   POWER MEASUREMENT IN SONOCHEMISTRY [J].
CONTAMINE, RF ;
WILHELM, AM ;
BERLAN, J ;
DELMAS, H .
ULTRASONICS SONOCHEMISTRY, 1995, 2 (01) :S43-S47
[9]   EFFECT OF CAVITATION ON REACTING SYSTEMS [J].
COUPPIS, EC ;
KLINZING, GE .
AICHE JOURNAL, 1974, 20 (03) :485-491
[10]   Direct sonication system suitable for medium-scale sonochemical reactors [J].
Dahlem, O ;
Demaiffe, V ;
Halloin, V ;
Reisse, J .
AICHE JOURNAL, 1998, 44 (12) :2724-2730