SPARGED LOOP REACTORS

被引:141
作者
JOSHI, JB
RANADE, VV
GHARAT, SD
LELE, SS
机构
[1] Department of Chemical Technology, University of Bombay, Bombay, 400 019, Matunga Road
关键词
air lift; gas‐liquid interactions; loop reactors; sparging; two‐phase flows;
D O I
10.1002/cjce.5450680501
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Circulating bubble columns or loop reactors form one of the important classes of modified bubble columns. The present paper analyses the performance of external loop air lift reactors (EL‐ALR). The EL‐ALR has many advantageous features especially at large scale. These arise from its feature of having controlled liquid circulation which is the key parameter for the design and operation of EL‐ALR contactors. Therefore, a reliable and generalised circulation model has been presented. The reliability of the model depends on the accuracy of the predictive methods for the gas hold‐up and the two‐phase fractional pressure drop. Detailed analysis of these fundamental parameters of gas‐liquid flows has been presented. The effects of design (area ratio of riser to downcomer, height to diameter ratio and volume of reactor) and operating (gas flow rates and sparging locations) parameters on the performance of the EL‐ALR have been analysed in detail. A rational basis has been developed for the estimation of pressure drop, mixing time and mass transfer coefficient. An optimum combination of design and operating parameters has been suggested and a criterion has been developed for the optimum location of spargers. An attempt has been made to provide critical analysis of the published information and to construct a coherent picture of EL‐ALR. Copyright © 1990 Canadian Society for Chemical Engineering
引用
收藏
页码:705 / 741
页数:37
相关论文
共 136 条
  • [1] GAS HOLDUP AND VOLUMETRIC MASS-TRANSFER COEFFICIENT IN BUBBLE COLUMNS - EFFECTS OF LIQUID PROPERTIES
    AKITA, K
    YOSHIDA, F
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1973, 12 (01): : 76 - 80
  • [2] [Anonymous], [No title captured]
  • [3] AOKI S, 1965, 2ND P S HEAT TRANSF, P137
  • [4] ARMOND AA, 1950, IZU VTI, V2, P1
  • [5] Bach H., 1978, GER CHEM ENG, V1, P270
  • [6] BARNEA D, 1987, ENCY FLUID MECHANICS, V3, P403
  • [7] GAS HOLDUP AND OVERALL VOLUMETRIC OXYGEN-TRANSFER COEFFICIENT IN AIRLIFT CONTACTORS
    BELLO, RA
    ROBINSON, CW
    MOOYOUNG, M
    [J]. BIOTECHNOLOGY AND BIOENGINEERING, 1985, 27 (03) : 369 - 381
  • [8] PREDICTION OF THE VOLUMETRIC MASS-TRANSFER COEFFICIENT IN PNEUMATIC CONTACTORS
    BELLO, RA
    ROBINSON, CW
    MOOYOUNG, M
    [J]. CHEMICAL ENGINEERING SCIENCE, 1985, 40 (01) : 53 - 58
  • [9] BELLO RA, 1984, CAN J CHEM ENG, V62, P573, DOI DOI 10.1002/CJCE.5450620501
  • [10] PREDICTION OF BUBBLE CONCENTRATION PROFILES IN VERTICAL TURBULENT 2-PHASE FLOW
    BEYERLEIN, SW
    COSSMANN, RK
    RICHTER, HJ
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1985, 11 (05) : 629 - 641