Modeling hydrodynamic cavitation in venturi: influence of venturi configuration on inception and extent of cavitation

被引:58
作者
Simpson, Alister [1 ]
Ranade, Vivek V. [1 ]
机构
[1] Queens Univ Belfast, Sch Chem & Chem Engn, Belfast BT9 5AG, Antrim, North Ireland
关键词
hydrodynamic cavitation; venturi; CFD; multiphase; unsteady flows; EFFICIENT PRETREATMENT; WASTE-WATER; DEGRADATION; REACTOR; FLOW; INTENSIFICATION; OPTIMIZATION; BIOMASS;
D O I
10.1002/aic.16411
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrodynamic cavitation (HC) is useful for intensifying a wide variety of industrial applications including biofuel production, emulsion preparation, and wastewater treatment. Venturi is one of the most widely used devices for HC. Despite the wide spread use, the role and interactions among various design and operating parameters on generated cavitation is not yet adequately understood. This article presents results of computational investigation into the cavitation characteristics of different venturi designs over a range of operating conditions. Influence of the key geometric parameters such as the length of venturi throat and diffuser angle on the inception and extent of cavitation is discussed quantitatively. Formulation and solution of multiphase computational fluid dynamics (CFD) models are presented. Appropriate turbulence and cavitation models are selected and solved using a commercial CFD code. Care was taken to eliminate the influence of numerical parameters like mesh density, discretization scheme, and convergence criteria. The computational model was validated by comparing simulated results with three published data sets. The simulated results in terms of velocity and pressure gradients, vapor volume fractions and turbulence quantities, and so on, are critically analyzed and discussed. Diffuser angle was found to have a significant influence on cavitation inception and evolution. The length of the venturi throat has relatively less impact on cavitation inception and evolution compared to the diffuser angle. The models and simulated flow field were used to simulate detailed time-pressure histories for individual vapor cavities, including turbulent fluctuations. This in turn can be used to simulate cavity collapse and overall performance of HC device as a reactor. The presented results offer useful guidance to the designer of HC devices, identifying key operating and design parameters that can be manipulated to achieve the desired level of cavitational activity. The presented approach and results also offer a useful means to compare and to evaluate different designs of cavitation devices and operating parameters. (c) 2018 American Institute of Chemical Engineers AIChE J, 65: 421-433, 2019
引用
收藏
页码:421 / 433
页数:13
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