PREDICTION OF LIQUID-FILM MASS-TRANSFER COEFFICIENTS IN PACKED-COLUMNS USING LIQUID HOLDUP

被引:0
作者
RAO, KR
机构
关键词
RANDOM PACKED COLUMNS; LIQUID HOLDUP; CORRELATION; LIQUID FILM MASS TRANSFER COEFFICIENT;
D O I
暂无
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A unique characteristic linear dimension (d), defined as the cube root of the specific liquid holdup (h(sp)) in the packed column, was used to correlate successfully the liquid film mass transfer coefficient k(L)a for gas absorption-desorption for sparingly soluble gases in liquids below loading. To produce this simple, dimensionless correlation, k(L)a data reported in literature were used, covering a wide range of physical properties of liquids, packings and operating conditions. This new approach showed operating holdup as an important factor in gas liquid mass transfer.
引用
收藏
页码:685 / 688
页数:4
相关论文
共 24 条
[1]   ESTIMATION OF LIQUID-FILM MASS-TRANSFER COEFFICIENTS FOR RANDOMLY PACKED ABSORPTION COLUMNS [J].
AUYEUNG, PH ;
PONTER, AB .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1983, 61 (04) :481-493
[2]  
BENNETT A, 1970, TRANS INST CHEM ENG, V48, pT232
[3]  
DAVIDSON JF, 1959, T I CHEM ENGRS, V37, P131
[4]  
DED DW, 1947, IND ENG CHEM, V39, P766
[5]   Liquid holdup and flooding in packed towers [J].
Elgin, JC ;
Weiss, FB .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1939, 31 :435-445
[6]   AXIAL MIXING OF LIQUID IN GAS-LIQUID FLOW THROUGH PACKED BEDS [J].
HOOGENDO.CJ ;
LIPS, J .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1965, 43 (03) :125-&
[7]  
Jesser BW, 1943, T AM INST CHEM ENG, V39, P0277
[8]   A RESIDENCE-TIME MODEL FOR TRICKLE-FLOW REACTORS INCORPORATING INCOMPLETE MIXING IN STAGNANT REGIONS [J].
KAN, KM ;
GREENFIELD, PF .
AICHE JOURNAL, 1983, 29 (01) :123-132
[9]  
KOCH HA, 1949, CHEM ENG PROG, V45, P677
[10]   LIQUID HOLDUP AND DISPERSION IN PACKED-COLUMNS [J].
KUSHALKAR, KB ;
PANGARKAR, VG .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (03) :759-763