Bubble characteristics measured using a monofibre optical probe in a bubble column and freeboard region under high gas holdup conditions

被引:56
作者
Pjontek, Dominic [1 ]
Parisien, Valois [1 ]
Macchi, Arturo [1 ]
机构
[1] Univ Ottawa, Ctr Catalysis Res & Innovat, Dept Chem & Biol Engn, Ottawa, ON K1N 6N5, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Bubble properties; Optical probe; Bubble column; Gas holdup; High pressure; Surfactant; FLUIDIZED-BED; VOID FRACTION; LOCAL MEASUREMENTS; ELEVATED PRESSURE; FIBER PROBE; LIQUID; VELOCITY; DYNAMICS; SINGLE; SIZE;
D O I
10.1016/j.ces.2014.02.024
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Local bubble characteristics, including gas holdups, bubble rise velocities, and chord lengths, were measured using a monolibre optical probe manufactured to withstand elevated pressures. Previous studies have validated the use of single tip probes for simultaneous measurement of local bubble properties at atmospheric conditions; however no study has been currently reported for these probes at elevated pressures. Experiments were conducted in a 101.6 mm diameter column operating at pressures up to 9.0 MPa. Surfactant addition and operating pressure were studied to simulate high gas holdups observed in many industrial reactors containing liquid mixtures with surface-active compounds. Experiments were hence completed using two liquid phases: tap water and a 0.5 wt% aqueous ethanol solution. Liquid and gas superficial velocities were varied between 0-90 mm/s and 0-150 mm/s, respectively. Radial profiles at atmospheric conditions validated the probe measurements in water. Local holdups, rise velocities and chord lengths were adequately measured in water up to 9.0 MPa. The probe struggled in the aqueous ethanol solution due to its physical constraints (i.e., Lip diameter and sensing length) when compared to the significant bubble size reduction (chord lengths below 0.5 mm). Comparisons with fluidized bed freeboard measurements demonstrated that flow through the bed enhanced bubble breakup for a coalescing system, but had a negligible impact with the added surfactant. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:153 / 169
页数:17
相关论文
共 47 条
[31]   A new contact time model for the mechanistic assessment of local heat transfer coefficients in bubble column using both the four-optical fiber probe and the fast heat transfer probe-simultaneously [J].
Kagumba, Moses ;
Al-Naseri, Hayder ;
Al-Dahhan, Muthanna H. .
CHEMICAL ENGINEERING JOURNAL, 2019, 361 :67-79
[32]   Statistical Analysis of Experimental Variables on Gas Holdup in Novel Bubble Column Using Box-Behnken Design [J].
Dhanasekaran, S. ;
Karunanithi, T. .
INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2012, 10
[33]   Bubble Dynamics in 2D Bubble Column: Comparison between High-Speed Camera Imaging Analysis and 4-Point Optical Probe [J].
Ahmed, Fadha Shakir ;
Sensenich, Brent A. ;
Gheni, Saba A. ;
Znerdstrovic, Daniel ;
Al Dahhan, Muthanna H. .
CHEMICAL ENGINEERING COMMUNICATIONS, 2015, 202 (01) :85-95
[34]   Novel correlations for gas holdup in large-scale slurry bubble column reactors operating under elevated pressures and temperatures [J].
Behkish, A ;
Lemoine, R ;
Oukaci, R ;
Morsi, BI .
CHEMICAL ENGINEERING JOURNAL, 2006, 115 (03) :157-171
[35]   Gas-Liquid Mass Transfer Characteristics in a Gas-Liquid-Solid Bubble Column under Elevated Pressure and Temperature [J].
Jin, Haibo ;
Yang, Suohe ;
He, Guangxiang ;
Liu, Delin ;
Tong, Zemin ;
Zhu, Jianhua .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2014, 22 (09) :955-961
[36]   Direct estimation of gas holdup in gas-liquid bubble column reactors using ultrasonic transmission tomography and artificial neural processing [J].
Hu, Jingyi ;
Li, Nan ;
Wang, Lina ;
Yang, Peng ;
Yang, Yunjie ;
Quan, Yihong .
MEASUREMENT SCIENCE AND TECHNOLOGY, 2022, 33 (07)
[37]   Modeling gas holdup in a multiphase oxygen slurry bubble column reactor for Cu-Cl hydrogen production using CFD [J].
Abdulrahman, M. W. .
RESULTS IN ENGINEERING, 2024, 24
[38]   Gas-Liquid Mass Transfer in a Slurry Bubble Column Reactor under High Temperature and High Pressure [J].
杨卫国 ;
王金福 ;
金涌 .
Chinese Journal of Chemical Engineering, 2001, (03) :29-33
[39]   Gas-liquid mass transfer in a slurry bubble column reactor under high temperature and high pressure [J].
Yang, WG ;
Wang, JF ;
Jin, Y .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2001, 9 (03) :253-257
[40]   Thermally activated serpentine leaching under flue gas conditions in a bubble column reactor operated at ambient pressure and temperature [J].
Tebbiche, Ilies ;
Pasquier, Louis-Cesar ;
Mercier, Guy ;
Blais, Jean-Francois ;
Kentish, Sandra .
HYDROMETALLURGY, 2020, 195