NUMERICAL-CALCULATIONS FOR ASYMPTOTIC, DIFFUSION DOMINATED MASS-TRANSFER COEFFICIENT IN PACKED-BED REACTORS

被引:6
作者
FEDKIW, P [1 ]
NEWMAN, J [1 ]
机构
[1] UNIV CALIF BERKELEY,DEPT CHEM ENGN,BERKELEY,CA 94720
关键词
D O I
10.1016/0009-2509(78)85212-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
引用
收藏
页码:1563 / 1566
页数:4
相关论文
共 5 条
[1]   LOW PECLET NUMBER BEHAVIOR OF TRANSFER RATE IN PACKED-BEDS [J].
FEDKIW, P ;
NEWMAN, J .
CHEMICAL ENGINEERING SCIENCE, 1978, 33 (08) :1043-1048
[2]   MASS-TRANSFER AT HIGH PECLET NUMBERS FOR CREEPING FLOW IN A PACKED-BED REACTOR [J].
FEDKIW, P ;
NEWMAN, J .
AICHE JOURNAL, 1977, 23 (03) :255-263
[3]  
Newman J., 1977, ELECTROCHEMICAL SYST
[4]   NEW MODEL FOR GRANULAR POROUS MEDIA - MODEL FORMULATION [J].
PAYATAKES, AC ;
TIEN, C ;
TURIAN, RM .
AICHE JOURNAL, 1973, 19 (01) :58-67
[5]   COMPUTATION OF FORCED-CONVECTION IN SLOW FLOW THROUGH DUCTS AND PACKED-BEDS .3. HEAT AND MASS-TRANSFER IN A SIMPLE CUBIC ARRAY OF SPHERES [J].
SORENSEN, JP ;
STEWART, WE .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (03) :827-832