Simulation and experimental validation of Taylor-Couette flow in square cross-section container for water treatment reactor

被引:2
作者
Sierra-Espinosa, F. Z. [1 ]
Escamilla-Ruiz, I. A. [1 ]
Rodriguez, Mayte L. [1 ]
Alvarez-Gallegos, A. [1 ]
Carrillo, F. [1 ]
Teloxa, J. [2 ]
机构
[1] UAEM, CIICAp, Ave Univ 1001, Cuernavaca 62209, Morelos, Mexico
[2] Univ Politecn Tlaxcala, Dept Ingn Ind, Ave Univ Politecn 1, Tepeyanco 90180, Tlaxcala, Mexico
关键词
Taylor-Couetteflow; PIV velocimetry; Stirring; Square container; Thermal analysis; Turbulence intensity; ANNULAR CENTRIFUGAL EXTRACTORS; 3-DIMENSIONAL CFD SIMULATION; STIRRED-TANK; VORTEX FLOW; SCALE-UP; ROTATING CYLINDERS; PIV INTERROGATION; ENERGY; INSTABILITIES; BIOREACTOR;
D O I
10.5004/dwt.2017.20707
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A vortex flow developed by a rotational cylindrical rod centrally placed in a container of square cross section was investigated experimentally and numerically. This configuration was analyzed given its potential use in water treatment. We focused the analysis on a relation of inner radius and side length L/r = 7.33. This ratio represents a warranty for vortex flow stability. Large ratios have the advantage of handling larger volumes with a sustained control of residence. The study was based on measuring velocity using particle image velocimetry, PIV and modelling the flow by computational fluid dynamics (CFD). Taylor-Couette cells on laminar-turbulent regimes developed for all the rotating conditions examined with Reynolds numbers between 2750 and 4950. The measurements revealed that turbulence intensity Tu increases in the radial direction towards the corners. This is by interaction fluid-walls, where corners act as natural baffles. Numerical simulations showed that secondary flows develop in the corners, with high levels of turbulence, which is important for mixing. It is shown that present configuration consumes less energy than a Taylor-Couette flow from classical concentric-cylinder systems. Heat transfer rate produced by imposed temperature conditions on the walls of the container affect vortex size and position modifying the flow structure observed in the pure dynamics case. The results indicate that configurations like square container-rotating cylinder may enhance water treatment.
引用
收藏
页码:353 / 372
页数:20
相关论文
共 55 条
  • [1] Two-fluid Taylor-Couette flow: Experiments and linear theory for immiscible liquids between corotating cylinders
    Baier, G
    Graham, MD
    [J]. PHYSICS OF FLUIDS, 1998, 10 (12) : 3045 - 3055
  • [2] Bakker A., 1993, AICHE S SERIES, V299, P71
  • [3] Theoretical and experimental study of the effects of scale-up on mixing time for a stirred-tank bioreactor
    Bonvillani, P
    Ferrari, MP
    Ducrós, EM
    Orejas, JA
    [J]. BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2006, 23 (01) : 1 - 7
  • [4] Ch S., 2006, INT COMMUN HEAT MASS, V33, P737
  • [5] Chtourou W., 2014, ENERGY POWER ENG, V06, P95, DOI [10.4236/epe.2014.65010, DOI 10.4236/EPE.2014.65010]
  • [6] ANALYSIS OF A ROTATING ANNULAR REACTOR IN THE VORTEX FLOW REGIME
    COHEN, S
    MARON, DM
    [J]. CHEMICAL ENGINEERING SCIENCE, 1991, 46 (01) : 123 - 134
  • [7] Coleman HW., 2018, EXPT VALIDATION UNCE
  • [8] Steady mixed convection in a differentially heated square enclosure with an active rotating circular cylinder
    Costa, V. A. F.
    Raimundo, A. M.
    [J]. INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2010, 53 (5-6) : 1208 - 1219
  • [9] Dantec Dynamics Inc, 2009, PART IM VEL SYST FLO
  • [10] Large-eddy simulation of single-phase flow dynamics and mixing in an industrial crystallizer
    Derksen, J. J.
    Kontomaris, K.
    McLaughlin, J. B.
    Van den Akker, H. E. A.
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2007, 85 (A2) : 169 - 179