EXPERIENCE GAINED WITH A NEW METHOD FOR CALCULATIONS ON COUNTERCURRENT SEPARATION PROCESSES

被引：6

作者：

KETCHUM, RG

机构：

来源：

关键词：

D O I：

10.1002/cite.330430508

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：264 / &

共 11 条

AMUNDSON, NR ;

PONTINEN, AJ .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1958, 50 (05) :730-736

[2] Design for hydrocarbon absorption and stripping [J].

Edmister, WC .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1943, 35 :837-839

Lewis, WK ;

Matheson, GL .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1932, 24 :494-498

[4]

Lyster W. N., 1959, PETROL REFINER, V38, P151

[5]

LYSTER WN, 1959, PETROL REFINER, V38, P139

[6]

LYSTER WN, 1959, PETROL REFINER, V38, P221

[7] CONTINUOUS DISTILLATION CALCULATIONS BY RELAXATION METHOD [J].

ROSE, A ;

SWEENY, RF ;

SCHRODT, VN .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1958, 50 (05) :737-740

[8]

STAINTHORP FP, 1967, T I CHEM ENGR S, V73, P189

[9]

STAINTHORP FP, 1967, T I CHEM ENGRS S SER, V73, P181

[10] Computation of distillation apparatus for hydrocarbon mixtures [J].

Thiele, EW ;

Geddes, RL .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1933, 25 :289-295