VAPOR-LIQUID EQUILIBRIA IN 3 HYDROGEN-PARAFFIN SYSTEMS

[1] BRIDGEMAN OC, 1930, P AM PETROLEUM I, V11, P4

[2] Solubilities of gases in liquids at high pressure [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1931, 23 : 548 - 550

[3] IPATIEFF VV, 1935, J PHYS CHEM-US, V6, P632

[4] IPATIEFF VV, 1937, CHEM SOLID FUELS, V8, P866

[5] Vaporization equilibrium constants in a crude oil-natural gas system [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1937, 29 : 1072 - 1077

[6] KATZ WB, 1941, CHEM REV, V29, P501

[7] Solubility of hydrogen in n-butane [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1943, 35 : 204 - 206

[8] SAGE BH, 1938, IND ENG CHEM, V30, P679

[9] Boiling points of n-heptane and 2,2,4-trimethylpentane over the range 100-to 1,500-millimeter pressure [J]. JOURNAL OF RESEARCH OF THE NATIONAL BUREAU OF STANDARDS, 1940, 24 (03): : 229 - 234

[1] BRIDGEMAN OC, 1930, P AM PETROLEUM I, V11, P4

[2] Solubilities of gases in liquids at high pressure [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1931, 23 : 548 - 550

[3] IPATIEFF VV, 1935, J PHYS CHEM-US, V6, P632

[4] IPATIEFF VV, 1937, CHEM SOLID FUELS, V8, P866

[5] Vaporization equilibrium constants in a crude oil-natural gas system [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1937, 29 : 1072 - 1077

[6] KATZ WB, 1941, CHEM REV, V29, P501

[7] Solubility of hydrogen in n-butane [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1943, 35 : 204 - 206

[8] SAGE BH, 1938, IND ENG CHEM, V30, P679

[9] Boiling points of n-heptane and 2,2,4-trimethylpentane over the range 100-to 1,500-millimeter pressure [J]. JOURNAL OF RESEARCH OF THE NATIONAL BUREAU OF STANDARDS, 1940, 24 (03): : 229 - 234