Intrinsic Hydrodynamic Investigation of Three-Phase Bubble Column: Comparative Experimental Study on Gas Holdup

被引:7
|
作者
Asil, A. Garmroodi [1 ]
Pour, A. Nakhaei [2 ]
Mirzaei, Sh. [3 ]
机构
[1] Univ Bojnord, Chem Engn Dept, Fac Engn, Bojnord, Iran
[2] Ferdowsi Univ Mashhad, Fac Basic Sci, Chem Dept, Mashhad, Razavi Khorasan, Iran
[3] Ferdowsi Univ Mashhad, Chem Engn Dept, Fac Engn, Mashhad, Razavi Khorasan, Iran
关键词
hydrodynamics; gas holdup; slurry bubble column; sparger; superficial gas velocity; MASS-TRANSFER COEFFICIENTS; FISCHER-TROPSCH SYNTHESIS; SCALE-UP; REACTOR; SIZE; TEMPERATURE; TRANSITION; CATALYST; LIQUIDS; DESIGN;
D O I
10.1134/S0040579520020050
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A comprehensive experimental study of the hydrodynamic behaviors for the specific system of air/paraffin oil/silica particles in a slurry bubble column of 0.15 m diameter and 2.9 m length has been carried out. The effect of regime transition, solid concentrations, static liquid height, sparger type and related bubble size on gas holdup over a range of superficial gas velocities has been investigated. From the experimental work, it is revealed that the gas holdup increases by increasing the superficial gas velocity and transition regime occurred at 0.043 to 0.08 m/s. The slope of this curve is steeper for homogeneous regime and less for heterogeneous regime. In addition, the presence of silica particle (0-40 vol %) inhibits bubble breakage, increases rise velocity and consequently decreases residence time and gas holdup. Approximately a 40% decrease in the overall gas holdup was observed by adding 40% solid particles to the air/paraffin oil system. Moreover, increasing static liquid height from 6 to 12 leads to about a 61% decrease in gas holdup in the absence of solid particles. Also, the use of a perforated plate instead of a porous one causes a 9% increase and a 21% decrease in bubble size and gas holdup, respectively. Finally, it is found that the Krishna and Sie correlation can predict gas holdup in the air/paraffin oil/silica particles system with an acceptable minimum relative error of about 8%.
引用
收藏
页码:331 / 341
页数:11
相关论文
共 50 条
  • [1] Intrinsic Hydrodynamic Investigation of Three-Phase Bubble Column: Comparative Experimental Study on Gas Holdup
    A. Nakhaei A. Garmroodi Asil
    Sh. Pour
    Theoretical Foundations of Chemical Engineering, 2020, 54 : 331 - 341
  • [2] Experimental investigation and its analysis of gas holdup in a three-phase counter-current microstructured bubble column
    Prakash, Ritesh
    Bhattacharyya, Adhwarshu
    Majumder, Subrata Kumar
    JOURNAL OF DISPERSION SCIENCE AND TECHNOLOGY, 2022, 43 (02) : 243 - 258
  • [3] Influence of structured packing on gas holdup in a three-phase bubble column
    Monsalvo, Matias
    Boehm, Ursula
    CHEMICAL ENGINEERING SCIENCE, 2007, 62 (23) : 6595 - 6603
  • [4] Study of Gas Holdup for Bubble Column at Three Phases
    Hameed, Laith A.
    Muhammad, Omar
    Saad, Sarah
    Dahham, Omar S.
    Noriman, N. Z.
    Shayfu, Z.
    GREEN DESIGN AND MANUFACTURE: ADVANCED AND EMERGING APPLICATIONS, 2018, 2030
  • [5] Numerical Investigation of Gas Holdup and Phase Mixing in Bubble Column Reactors
    Bai, Wei
    Deen, Niels G.
    Kuipers, J. A. M.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (04) : 1949 - 1961
  • [6] Holdup and velocity profiles of monosized spherical solids in a three-phase bubble column
    Gan, Z. W.
    CHEMICAL ENGINEERING SCIENCE, 2013, 94 : 291 - 301
  • [7] GAS HOLDUP IN TWO - AND THREE-PHASE DOWNFLOW BUBBLE COLUMNS.
    Shah, Y.T.
    Kulkarni, A.A.
    Wieland, J.H.
    Carr, N.L.
    1600, (26):
  • [8] Gas phase holdup in slurry bubble columns for two- and three-phase systems
    Saxena, S.C.
    Rao, N.S.
    Thimmapuram, P.R.
    1600, (49):
  • [9] Prediction of gas-phase holdup in a bubble column
    Zhu, JW
    Saxena, SC
    CHEMICAL ENGINEERING COMMUNICATIONS, 1997, 161 : 149 - 161
  • [10] A comparative study of gas holdup, bubble size distribution and interfacial area in a downflow bubble column
    Mandal, A
    Kundu, G
    Mukherjee, D
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2005, 83 (A4): : 423 - 428