Using tomography to visualize the continuous-flow mixing of biopolymer solutions inside a stirred tank reactor

被引:22
|
作者
Patel, Dineshkumar [1 ]
Ein-Mozaffari, Farhad [1 ]
Mehrvar, Mehrab [1 ]
机构
[1] Ryerson Univ, Dept Chem Engn, Toronto, ON M5B 2K3, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Mixing; Non-Newtonian fluids; Yield stress; Laminar flow; Transitional flow; Tomography; ELECTRICAL-RESISTANCE TOMOGRAPHY; NON-NEWTONIAN FLUIDS; LASER-DOPPLER VELOCIMETRY; APPLIED POTENTIAL TOMOGRAPHY; POSSESSING YIELD-STRESS; PULP STOCK CHESTS; MAXBLEND IMPELLER; DYNAMIC TESTS; RESIDENCE TIME; AGITATED TANKS;
D O I
10.1016/j.cej.2013.11.007
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The vast majority of non-Newtonian fluids are naturally opaque; therefore, visualizing the flow field of such fluids inside a reactor is a challenging task. To identify non-ideal flows, such as dead volumes and channeling, in a continuous-flow mixing system, the flow field inside a stirred tank reactor was visualized using electrical resistance tomography (ERT), an efficient non-intrusive measurement technique. The key objective of this study was to employ the ERT technique in order to explore the effects of the inlet and outlet locations (four configurations: top inlet-bottom outlet, bottom inlet-top outlet, bottom inlet-bottom outlet, and top inlet-top outlet), fluid rheology (0.5-1.5% xanthan gum concentration), jet velocity (0.317-1.660 m s(-1)), feed flow rate (5.3 x 10(-5)-2.36 x 10(-4) M-3 s(-1)), impeller type (the Rushton turbine and Maxblend impellers), and impeller speed (54-250 rpm) on the flow patterns generated in the continuous-flow mixing of the xanthan gum solution, which is a pseudoplastic fluid exhibiting yield stress. Using 2D and 3D tomography images, this article effectively presents a competent method to visualize the flow of opaque fluids in laminar and transitional regions inside a reactor. In this study, the existence of non-ideal flows in a stirred tank reactor for opaque fluids was identified using ERT. The quantitative results showed that the tracer distribution (or mixing quality) inside stirred vessel was enhanced by decreasing the fluid yield stress, increasing the impeller speed, increasing the jet velocity, and using the close clearance impeller. The results also showed that the location of the inlet and outlet streams has a significant effect on the mixing quality. To improve the design of the continuous-flow mixing of non-Newtonian fluids, the findings of this study can be integrated into the design criteria to achieve optimal mixing results. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:257 / 273
页数:17
相关论文
共 50 条
  • [1] MIXING MODEL FOR A CONTINUOUS-FLOW STIRRED TANK REACTOR
    HANLEY, TR
    MISCHKE, RA
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1978, 17 (01): : 51 - 58
  • [2] MIXING PHENOMENA IN A CONTINUOUS-FLOW STIRRED TANK REACTOR
    BURGHARDT, A
    LIPOWSKA, L
    [J]. CHEMICAL ENGINEERING SCIENCE, 1972, 27 (10) : 1783 - +
  • [3] A MIXING MODEL FOR A CONTINUOUS-FLOW STIRRED TANK REACTOR - COMMENTS
    DAVID, R
    VILLERMAUX, J
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1980, 19 (03): : 326 - 327
  • [4] A MIXING MODEL FOR A CONTINUOUS-FLOW STIRRED TANK REACTOR - COMMENTS
    LIEKHUS, KJ
    HANLEY, TR
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1986, 25 (01): : 177 - 179
  • [5] Liquid mixing in a continuous-flow, stirred-tank reactor
    Kim, T.O.
    Kang, W.K.
    [J]. International chemical engineering, 1988, 28 (04): : 690 - 697
  • [6] A MIXING MODEL FOR A CONTINUOUS-FLOW STIRRED TANK REACTOR - REPLY
    DAVID, R
    VILLERMAUX, J
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1986, 25 (01): : 179 - 180
  • [7] MIXING AND RECYCLE FOR ANALYSIS OF A CONTINUOUS-FLOW STIRRED TANK
    ANANDHA, M
    BRODKEY, RS
    [J]. CHEMICAL ENGINEERING SCIENCE, 1972, 27 (12) : 2199 - &
  • [8] Effects of mixing on parallel chemical reactions in a continuous-flow stirred-tank reactor
    Baldyga, J
    Henczka, M
    Makowski, L
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2001, 79 (A8): : 895 - 900
  • [9] TEMPERATURE-GRADIENTS IN A CONTINUOUS-FLOW STIRRED TANK REACTOR
    AZAY, P
    COME, GM
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1979, 18 (04): : 754 - 756
  • [10] Effects of turbulent mixing on parallel chemical reactions in a continuous-flow stirred-tank reactor
    Baldyga, J
    Henczka, M
    Makowski, L
    [J]. INZYNIERIA CHEMICZNA I PROCESOWA, 2001, 22 (3B): : 199 - 204