430288 CFD Simulations of a Stirred Tank Reactor for Liquid and Gas-Liquid Systems Using OpenfoamŪ

Tuesday, November 10, 2015: 3:57 PM
Salon H (Salt Lake Marriott Downtown at City Creek)
Xiaofei Hu1, Alberto Passalacqua1 and Rodney O. Fox2, (1)Mechanical Engineering, Iowa State University, Ames, IA, (2)Chemical and Biological Engineering, Iowa State University, Ames, IA

Stirred tank reactors are widely used in industrial processes, including chemical processes like polymerization, biological processes such as cell culture and fermentation, pharmaceutical industry, and many other processes. Multiple impellers are usually preferred over single impeller for tall-thin configuration of industrial reactors for better gas utilization and maintenance of homogeneity in the reactor. In this work, the stirred tank reactor experimentally studied in Shewale and Pandit [1] is investigated numerically. The reactor is constituted by a cylindrical vessel with four baffles, and three impellers (one Rushton turbine, at the bottom of the tank, and two pitched blade turbines) mounted on the shaft and rotating synchronously.

A three-dimensional hexahedral mesh for the system is generated using a commercial mesh-generation software Pointwise®. CFD simulations are performed with the open-source CFD software OpenFOAM®. Steady state single-phase (liquid) simulations are performed with the realizable k-ε model, in order to describe the turbulence in the reactor. For gas-liquid system, a two-fluid model [2] with the mixture k-ε turbulence model [3] is used to solve the flow. The multiple reference frame approach [4] is applied for both systems to treat the rotation of impellers in the reactor. For both single phase and multiphase systems, the liquid phase is water at 300 K. And for multiphase system, air at 300 K is injected uniformly from the ring sparger located below the bottom Rushton turbine. Simulation results are compared to experiments reported in Shewale and Pandit [1], including flow patterns, unaerated and aerated power consumption, and overall gas holdup. The effects of different operating conditions such as impeller rotation speed at 3.75 rad/s and 5.08 rad/s are also studied.

[1] S.D. Shewale, A.B. Pandit, Studies in multiple impeller agitated gas–liquid contactors, Chemical Engineering Science. 61 (2006) 489–504.

[2] D.A. Drew, Mathematical modeling of two-phase flow, Annual Review of Fluid Mechanics. 15 (1983) 261–291.

[3] A. Behzadi, R.I. Issa, H. Rusche, Modelling of dispersed bubble and droplet flow at high phase fractions, Chemical Engineering Science. 59 (2004) 759–770.

[4] J. Luo, R. Issa, A. Gosman, Prediction of impeller induced flows in mixing vessels using multiple frames of reference, in: Institution of Chemical Engineers Symposium Series. 136 (1994) 549.

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See more of this Session: The Use of CFD in Simulation of Multiphase Mixing Processes
See more of this Group/Topical: North American Mixing Forum