CRITICAL TEMPERATURES OF TERNARY HYDROCARBON SYSTEMS

[1] [Anonymous], 1959, J CHEM ENG DATA

[2] PHASE BEHAVIOR IN THE METHANE-ETHANE-NORMAL-PENTANE SYSTEM [J]. TRANSACTIONS OF THE AMERICAN INSTITUTE OF MINING AND METALLURGICAL ENGINEERS, 1948, 174 : 13 - 24

[3] BLOOMER OT, 1953, 22 I GAS TECHN RES B

[4] COTA HM, 1960, THESIS NORTHWESTERN

[5] Phase behavior in the methane-propane-n-pentane system [J]. TRANSACTIONS OF THE AMERICAN INSTITUTE OF MINING AND METALLURGICAL ENGINEERS, 1943, 151 : 206 - 215

[6] Liquid-vapor equilibrium relations in binary systems - The ethane-n-butane system [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1940, 32 : 353 - 357

[7] MATSCHKE DE, 1962, THESIS NORTHWESTERN

[8] Phase equilibria in hydrocarbon systems - The propane-n-butane system in the critical region [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1940, 32 : 118 - 123

[9] Reamer H.H., 1960, J CHEM ENG DATA, V5, P44

[10] PHASE EQUILIBRIA IN HYDROCARBON SYSTEMS - NORMAL-BUTANE DECANE SYSTEM IN THE CONDENSED REGION [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1946, 38 (10): : 986 - 989

[1] [Anonymous], 1959, J CHEM ENG DATA

[2] PHASE BEHAVIOR IN THE METHANE-ETHANE-NORMAL-PENTANE SYSTEM [J]. TRANSACTIONS OF THE AMERICAN INSTITUTE OF MINING AND METALLURGICAL ENGINEERS, 1948, 174 : 13 - 24

[3] BLOOMER OT, 1953, 22 I GAS TECHN RES B

[4] COTA HM, 1960, THESIS NORTHWESTERN

[5] Phase behavior in the methane-propane-n-pentane system [J]. TRANSACTIONS OF THE AMERICAN INSTITUTE OF MINING AND METALLURGICAL ENGINEERS, 1943, 151 : 206 - 215

[6] Liquid-vapor equilibrium relations in binary systems - The ethane-n-butane system [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1940, 32 : 353 - 357

[7] MATSCHKE DE, 1962, THESIS NORTHWESTERN

[8] Phase equilibria in hydrocarbon systems - The propane-n-butane system in the critical region [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1940, 32 : 118 - 123

[9] Reamer H.H., 1960, J CHEM ENG DATA, V5, P44

[10] PHASE EQUILIBRIA IN HYDROCARBON SYSTEMS - NORMAL-BUTANE DECANE SYSTEM IN THE CONDENSED REGION [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1946, 38 (10): : 986 - 989