LIQUID OVERFLOW FROM VERTICAL CO-CURRENT FOAM COLUMNS

被引:17
作者
DESAI, D [1 ]
KUMAR, R [1 ]
机构
[1] INDIAN INST SCI,DEPT CHEM ENGN,BANGALORE 560012,KARNATAKA,INDIA
关键词
FOAMS; -; GASES; LIQUIDS; VISCOSITY;
D O I
10.1016/0009-2509(84)80084-6
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A new criterion to predict the liquid overflow rate from vertical co-current foam column has been suggested. This criterion is combined with a recent model for liquid holdup in semi-batch foams to generate an analysis for co-current foam columns. This study also presents experimental investigations on liquid overflow rate in the hitherto unexplored ranges of parameters. The variables studied are liquid viscosity, surface viscosity and superficial gas velocity. The suggested model is compared with both the published as well as present experimental data on the liquid overflow rate. The agreement between the two is found to be reasonably good.
引用
收藏
页码:1559 / 1570
页数:12
相关论文
共 26 条
  • [1] AKERS RJ, 1976, FOAMS
  • [2] Bikerman J. J., 1973, FOAMS
  • [3] FOAM FRACTIONATION - STANDARD SEPARATOR AND REFLUXING COLUMNS
    BRUNNER, CA
    LEMLICH, R
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1963, 2 (04): : 297 - &
  • [4] DERYAGIN B.V., 1964, FILM COATING THEORY
  • [5] LIQUID HOLDUP IN SEMI-BATCH CELLULAR FOAMS
    DESAI, D
    KUMAR, R
    [J]. CHEMICAL ENGINEERING SCIENCE, 1983, 38 (09) : 1525 - 1534
  • [6] THE SURFACE VISCOSITY OF SOLUBLE FILMS
    EWERS, WE
    SACK, RA
    [J]. AUSTRALIAN JOURNAL OF CHEMISTRY, 1954, 7 (01) : 40 - 54
  • [7] FANLO S., 1965, AM IND CHEM ENG I CH, V9, P75
  • [8] Goucher FS, 1922, PHILOS MAG, V44, P1002
  • [9] A MODEL AND EXPERIMENTAL RESULTS FOR DRAINAGE OF SOLUTION BETWEEN FOAM BUBBLES
    HAAS, PA
    JOHNSON, HF
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (02): : 225 - &
  • [10] FLOW REGIMES OF STABLE FOAMS
    HOFFER, MS
    RUBIN, E
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1969, 8 (03): : 483 - &