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

页码：16 / 24

页数：9

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 [J].

CRAIG, LC ;

HAUSMANN, W ;

AHRENS, EH ;

HARFENIST, EJ .

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 [J].

KLINKENBERG, A .

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 [J].

KLINKENBERG, A ;

LAUWERIER, HA ;

REMAN, GH .

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 [J].

KLINKENBERG, A .

CHEMICAL ENGINEERING SCIENCE, 1951, 1 (02) :86-93

[8]

OLDSHUE JY, 1952, CHEM ENG PROG, V48, P297

[9] HOLDUP AND APPROACH TO STEADY STATE [J].

PEPPARD, DF ;

PEPPARD, MA .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (01) :34-39

[10]

PERRY JH, 1950, CHEM ENG HDB, P713

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