CALCULATION OF LIQUID-LIQUID EXTRACTION PROCESSES

被引：18

作者：

SCHEIBEL, EG

机构：

来源：

INDUSTRIAL AND ENGINEERING CHEMISTRY | 1954年 / 46卷 / 01期

关键词：

D O I：

10.1021/ie50529a020

中图分类号：

O69 [应用化学];

学科分类号：

081704 ;

摘要：

引用

收藏

页码：16 / 24

页数：9

相关论文

共 18 条

[1] BARTELS CR, 1949, CHEM ENG PROG, V45, P589
[2] Craig L.C., 1950, TECHNIQUE ORGANIC CH, V3
[3] AUTOMATIC COUNTERCURRENT DISTRIBUTION EQUIPMENT
CRAIG, LC
HAUSMANN, W
AHRENS, EH
HARFENIST, EJ
[J]. ANALYTICAL CHEMISTRY, 1951, 23 (09) : 1236 - 1244
[4] Craig LC, 1944, J BIOL CHEM, V155, P519
[5] 2-COMPONENT SEPARATIONS BY DOUBLE-SOLVENT EXTRACTION - DIAGRAMS FOR DETERMINING OPERATING CONDITIONS
KLINKENBERG, A
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1953, 45 (03): : 653 - 657
[6] CALCULATION OF THE EFFICIENCY OF COUNTER-CURRENT STAGE-WISE MASS TRANSFER PROCESSES WITH CONSTANT DISTRIBUTION FACTOR, WHEN IN THE STATIONARY STATE .2. STAGE REQUIREMENTS FOR THE SEPARATION OF 2 COMPONENTS BY 2 SOLVENT EXTRACTION
KLINKENBERG, A
LAUWERIER, HA
REMAN, GH
[J]. CHEMICAL ENGINEERING SCIENCE, 1951, 1 (02) : 93 - 99
[7] CALCULATION OF THE EFFICIENCY OF COUNTER-CURRENT STAGE-WISE MASS TRANSFER PROCESSES WITH CONSTANT DISTRIBUTION FACTOR, WHEN IN THE STATIONARY STATE .1. DISTRIBUTION OF ONE COMPONENT ONLY
KLINKENBERG, A
[J]. CHEMICAL ENGINEERING SCIENCE, 1951, 1 (02) : 86 - 93
[8] OLDSHUE JY, 1952, CHEM ENG PROG, V48, P297
[9] HOLDUP AND APPROACH TO STEADY STATE
PEPPARD, DF
PEPPARD, MA
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (01): : 34 - 39
[10] PERRY JH, 1950, CHEM ENG HDB, P713