THE CRITICAL TEMPERATURES OF MULTICOMPONENT HYDROCARBON SYSTEMS

[1] AMICK EH, 1952, CHEM ENG PROG S SER, V48, P65

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

[3] [Anonymous], 1962, J CHEM ENG DATA

[4] LIQUID-VAPOR EQUILIBRIUM IN METHANE-ETHYLENE-ISOBUTANE SYSTEM [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1945, 37 (01): : 55 - 59

[5] BILLMAN GW, 1948, T AM I MINING MET EN, V114, P13

[6] BLOOMER OT, 1953, I GAS TECHNOL RES B, V22

[7] Cota H. M., 1962, J CHEM ENG DATA, V7, P62

[8] High-pressure rectification IIN-pentane-N-heptane system [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1933, 25 : 728 - 732

[9] Davis P, 1954, J PETROL TECHNOL, V201, P37

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

[1] AMICK EH, 1952, CHEM ENG PROG S SER, V48, P65

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

[3] [Anonymous], 1962, J CHEM ENG DATA

[4] LIQUID-VAPOR EQUILIBRIUM IN METHANE-ETHYLENE-ISOBUTANE SYSTEM [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1945, 37 (01): : 55 - 59

[5] BILLMAN GW, 1948, T AM I MINING MET EN, V114, P13

[6] BLOOMER OT, 1953, I GAS TECHNOL RES B, V22

[7] Cota H. M., 1962, J CHEM ENG DATA, V7, P62

[8] High-pressure rectification IIN-pentane-N-heptane system [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1933, 25 : 728 - 732

[9] Davis P, 1954, J PETROL TECHNOL, V201, P37

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