CHARACTERIZATION OF GAS-LIQUID PARAMETERS IN A DOWN-FLOW JET LOOP BUBBLE COLUMN

被引:31
|
作者
Mandal, Ajay [1 ]
机构
[1] Indian Sch Mines, Dept Petr Engn, Dhanbad 826004, Bihar, India
关键词
Bubble column; Down-flow; Bubble size; Interfacial area; Mass transfer coefficient; MASS-TRANSFER COEFFICIENT; INTERFACIAL AREA; HOLDUP DISTRIBUTION; ENTRAINMENT RATE; CHEMICAL METHODS; DISPERSED PHASE; SIZE; REACTORS; EJECTOR; HYDRODYNAMICS;
D O I
10.1590/S0104-66322010000200004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In order to characterize the gas-liquid parameters of a down-flow jet loop reactor, experiments were carried out to study the gas holdup, bubble sizes and their distribution, mass transfer area and mass transfer coefficient. The experiments were performed in the bubbly flow regime because of its stability and uniformity. Analysis of experimental data showed an unambiguous relationship between gas holdup, bubble size, bubble size distribution and interfacial area. It has also been found that gas holdup and interfacial area is a strong function of slip velocity. The variation of interfacial area and mass transfer coefficient were also analyzed and expressed as a function of operational and geometric parameters.
引用
收藏
页码:253 / 264
页数:12
相关论文
共 50 条
  • [41] Turbulent flow structure and bubble distribution in an axisymmetric nonisothermal impinging gas-liquid jet
    M. A. Pakhomov
    V. I. Terekhov
    Fluid Dynamics, 2017, 52 : 288 - 298
  • [42] Modelling of gas-liquid flow in bubble regime
    Lance, M
    Tran, ML
    Petersen, K
    REVUE DE L INSTITUT FRANCAIS DU PETROLE, 1996, 51 (02): : 279 - 289
  • [43] EFFECT OF BUBBLE BREAKUP ON THE PARAMETERS OF BUBBLY FLOW OF A GAS-LIQUID MIXTURE.
    Nevinskiy, V.V.
    Rozenblyum, V.I.
    Savel'yev, M.I.
    Fluid mechanics. Soviet research, 1985, 14 (06): : 119 - 123
  • [44] GAS-LIQUID MASS-TRANSFER IN THE BUBBLE COLUMN WITH VISCOELASTIC LIQUID
    SUH, IS
    SCHUMPE, A
    DECKWER, WD
    KULICKE, WM
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1991, 69 (02): : 506 - 512
  • [45] Gas holdup in homogeneous and heterogeneous gas-liquid bubble column reactors
    Sarrafi, A
    Jamialahmadi, M
    Müller-Steinhagen, H
    Smith, JM
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (01): : 11 - 21
  • [46] FLOW PATTERN AND GAS HOLD-UP IN BUBBLE COLUMN WITH LIQUID JET EJECTOR
    OTAKE, T
    TONE, S
    OGAWA, S
    KAGAKU KOGAKU RONBUNSHU, 1982, 8 (01) : 65 - 72
  • [47] MACROMIXING CHARACTERISTICS OF GAS-LIQUID JET LOOP REACTORS
    WARNECKE, HJ
    ACTA BIOTECHNOLOGICA, 1989, 9 (02): : 111 - 121
  • [48] Experimental study on a co-current gas-liquid down flow contractor with gas entrainment by a liquid jet
    Laboratoire d'Analyse Environementale des Procedes et des Systemes Industriels LAEPSI - INSA de Lyon, 20 av. A. Einstein, 69621, villeurbanne, France
    Chem. Eng. Technol., 12 (1043-1049):
  • [49] Experimental and Numerical Investigation of Gas-Liquid Flow in a Rectangular Bubble Column with Centralized Aeration Flow Pattern
    Sanchez-Forero, Diana I.
    Silva, Joao L., Jr.
    Silva, Marcela K.
    Bastos, C. S. C.
    Mori, Milton
    ICHEAP-11: 11TH INTERNATIONAL CONFERENCE ON CHEMICAL AND PROCESS ENGINEERING, PTS 1-4, 2013, 32 : 1561 - 1566
  • [50] APPLICATION OF AN ELECTRICAL CONDUCTIVITY MICROPROBE FOR THE CHARACTERIZATION OF BUBBLE BEHAVIOR IN GAS-LIQUID BUBBLE FLOW.
    Steinemann, Juergen
    Buchholz, Rainer
    Particle Characterization, 1984, 1 (03): : 102 - 107