LONGITUDINAL MIXING IN ORIFICE PLATE GAS-LIQUID REACTORS

被引：27

作者：

BISCHOFF, KB

PHILLIPS, JB

机构：

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1966年 / 5卷 / 04期

关键词：

D O I：

10.1021/i260020a013

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：416 / &

共 17 条

[1] LONGITUDINAL MIXING IN GAS-SPARGED TUBULAR VESSELS
ARGO, WB
COVA, DR
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1965, 4 (04): : 352 - &
[2] MASS TRANSFER IN A SPARGED CONTACTOR .I. PHYSICAL MECHANISMS AND CONTROLLING PARAMETERS
BRAULICK, WJ
FAIR, JR
LERNER, BJ
[J]. AICHE JOURNAL, 1965, 11 (01) : 73 - &
[3] Calderbank P., 1958, TRANS INST CHEM ENG, V36, P443
[4] Calderbank PH, 1962, T I CHEM ENGRS, V40, P3
[5] Hughmark G.A., 1962, CHEM ENG PROG, V58, P62
[6] LEVENSPIEL O, 1962, CHEMICAL REACTION EN
[7] Levenspiel O., 1964, ADV CHEM ENG, V4, P95
[8] REPRESENTATION AND EVALUATION OF RESIDENCE TIME DISTRIBUTIONS
NAOR, P
SHINNAR, R
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1963, 2 (04): : 278 - &
[9] CHARACTERISTICS OF SINGLE-+ MULTIPLE-HOLE ORIFICE PLATES FOR GAS-LIQUID REACTIONS
OTTMERS, DM
RASE, HF
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1964, 3 (02): : 106 - &
[10] PHILLIPS JB, 1965, THESIS U TEXAS