VAPOR-LIQUID-EQUILIBRIA IN 3 BINARY AND TERNARY-SYSTEMS COMPOSED OF N-BUTANE, BUTENE-1, AND BUTADIENE-1,3

被引：21

作者：

LAURANCE, DR ^{[1
]}

SWIFT, GW ^{[1
]}

机构：

[1] UNIV KANSAS,DEPT CHEM & PETR ENGN,LAWRENCE,KS 66044

来源：

关键词：

D O I：

10.1021/je60060a008

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

引用

页码：61 / 67

页数：7

共 19 条

[1] Canjar LN, 1967, THERMODYNAMIC PROPER
[2] DEAN MR, 1944, IND ENG CHEM ANAL ED, V16, P7
[3] HACHMUTH K, 1946, T AICHE, V12, P975
[4] KAHRE LC, 1972, HYDROCARBON PROCESS, V50, P94
[5] A METHOD FOR PHASE EQUILIBRIUM CALCULATIONS BASED ON GENERALIZED BENEDICT-WEBB-RUBIN CONSTANTS
KAUFMANN, TG
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1968, 7 (01): : 115 - &
[6] Pressure-volume-temperature relations for n-butane
Kay, WB
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1940, 32 : 358 - 360
[7] RELATIVE VOLATILITY OF PROPANE-PROPENE SYSTEM FROM 100-160-DEGREES-F
LAURANCE, DR
SWIFT, GW
[J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1972, 17 (03) : 333 - &
[8] LAURANCE DR, 1973, THESIS U KANSAS
[9] MANLEY DB, 1971, J CHEM ENG DATA, V16, P301
[10] MANLEY DB, 1968, THESIS U KANSAS