Time-series analysis of optical probe measurements in gas-liquid stirred tanks

被引:15
作者
Lee, Boung Wook [1 ]
Dudukovic, Milorad P. [1 ]
机构
[1] Washington Univ, Dept Energy Environm & Chem Engn, CREL, St Louis, MO 63130 USA
基金
美国国家科学基金会;
关键词
Time-series analysis; Optical probe; Gas-liquid stirred tank; Multiphase reactor; PHASE-FLUID DISCRIMINATION; VOID FRACTION DISTRIBUTION; LOCAL FIBEROPTIC PROBES; FILLED CAVITY STRUCTURES; BUBBLE VELOCITY; FLOW; SIZE; SIMULATION; PRESSURE; VESSEL;
D O I
10.1016/j.ces.2014.05.048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work reports our findings on the time and frequency domain analysis of the optical probe measurements in a lab scale gas-liquid stirred tank reactor alternatively equipped with (i) a standard Rushton turbine and (ii) a half circular blades disk turbine. Optical measurements are collected from the tapered (conical) ends of optical fibers at five radial positions on the impeller discharge plane in the tank, r = 0.4 R, 0.5 R, 0.6 R, 0.7 R, 0.8 R, at a range of operating conditions. The collected data are processed and analyzed in the time and the frequency domains via MATLAB algorithms developed in house. The time domain analysis provided useful dispersion parameters, such as the local gas phase holdup and the bubble count, and the frequency domain analysis revealed information regarding the chaotic nature of bubble occupancy as a function of position and operating conditions. For both systems, the distinct pattern of the bubbles generated by the blades became chaotic beyond certain distances from the impeller at all operating conditions. In the vicinity of the impeller, however, different patterns are observed for the two turbines. These results suggest the optical probe's potential usage as a tool for impeller design and for in-situ identification/detection of the flow regime transitions to the fully recirculated regime. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:623 / 634
页数:12
相关论文
共 57 条
[1]  
Azzopardi BJ, 2011, HYDRODYNAMICS OF GAS-LIQUID REACTORS: NORMAL OPERATION AND UPSET CONDITIONS, P1, DOI 10.1002/9781119970712
[2]  
BAKKER A, 1994, CHEM ENG RES DES, V72, P594
[3]  
BAKKER A, 1994, CHEM ENG-NEW YORK, V101, P98
[4]   Solid suspension in a boiling stirred tank with radial flow turbines [J].
Bao, Yuyun ;
Gao, Zhengming ;
Li, Zhipeng ;
Bai, Ding ;
Smith, John M. ;
Thorpe, Rex B. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (07) :2420-2427
[5]   Individual impeller flooding in aerated vessel stirred by multiple-Rushton impellers [J].
Bombac, A ;
Zun, I .
CHEMICAL ENGINEERING JOURNAL, 2006, 116 (02) :85-95
[6]   Gas-filled cavity structures and local void fraction distribution in aerated stirred vessel [J].
Bombac, A ;
Zun, I ;
Filipic, B ;
Zumer, M .
AICHE JOURNAL, 1997, 43 (11) :2921-2931
[7]   Gas-filled cavity structures and local void fraction distribution in vessel with dual-impellers [J].
Bombac, A ;
Zun, I .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (15) :2995-3001
[8]   Multidimensional population balance model for the simulation of turbulent gas-liquid systems in stirred tank reactors [J].
Buffo, A. ;
Vanni, M. ;
Marchisio, D. L. .
CHEMICAL ENGINEERING SCIENCE, 2012, 70 :31-44
[9]   OPTICAL PROBES FOR LOCAL VOID FRACTION MEASUREMENTS - CHARACTERIZATION OF PERFORMANCE [J].
CARTELLIER, A .
REVIEW OF SCIENTIFIC INSTRUMENTS, 1990, 61 (02) :874-886
[10]   SIMULTANEOUS VOID FRACTION MEASUREMENT, BUBBLE VELOCITY, AND SIZE ESTIMATE USING A SINGLE OPTICAL PROBE IN GAS-LIQUID 2-PHASE FLOWS [J].
CARTELLIER, A .
REVIEW OF SCIENTIFIC INSTRUMENTS, 1992, 63 (11) :5442-5453