The decreasing solubility of hydrogen in hydrocarbons with decreasing temperature continues down to the freezing point of the hydrocarbons, around −300°F. This behavior is shown to be an enlargement of phenomena exhibited by normal hydrocarbon mixtures. Methods of predicting equilibrium-phase compositions are presented for hydrogen in ligh-hydrocarbon systems. The correlations are satisfactory for binary and certain ternary systems, but are not reliable for complex mixtures.Peer Reviewedhttp://deepblue.lib.umich.edu/bitstream/2027.42/37292/1/690030219_ftp.pd
The gas-liquid solubility of hydrogen in methanol, ethanol, 1-propanol, and 1-butanol at pressures i...
Owing to the highly supercritical nature of hydrogen in hydrogen-hydrocarbon systems, it is difficul...
Monte Carlo simulations were used to calculate water- methane and water- ethane phase equilibria ove...
Experimental equilibrium vapor and liquid compositions are reported for the hydrogen-methane system ...
Under previous support from the Department of Energy, an experimental facility has been established ...
Under previous support from the Department of Energy, an experimental facility has been established ...
Because of increased interest in coal conversion processes there is a growing need for basic informa...
In industry today, there remains a need for basic information on the fluid-phase equilibrium of mixt...
Development of high pressure-high temperature (RPHT) reservoirs is increasingly being pursued world ...
Under previous support from the Department of Energy, an experimental facility has been established ...
I t is common for the mutual solubility of a pair of liquids to increase with temperature until misc...
The inevitable presence of water in high pressure-high temperature reservoirs leads to a number of n...
Liquid—vapor equilibrium phase compositions for the binary system normal hydrogen—helium have been d...
This paper presents vapor-liquid equilibrium data for the system hydrogen—benzene—cyclohexane— n -he...
Experiments were performed to study the phase behavior of gas condensate hydrocarbons at ...
The gas-liquid solubility of hydrogen in methanol, ethanol, 1-propanol, and 1-butanol at pressures i...
Owing to the highly supercritical nature of hydrogen in hydrogen-hydrocarbon systems, it is difficul...
Monte Carlo simulations were used to calculate water- methane and water- ethane phase equilibria ove...
Experimental equilibrium vapor and liquid compositions are reported for the hydrogen-methane system ...
Under previous support from the Department of Energy, an experimental facility has been established ...
Under previous support from the Department of Energy, an experimental facility has been established ...
Because of increased interest in coal conversion processes there is a growing need for basic informa...
In industry today, there remains a need for basic information on the fluid-phase equilibrium of mixt...
Development of high pressure-high temperature (RPHT) reservoirs is increasingly being pursued world ...
Under previous support from the Department of Energy, an experimental facility has been established ...
I t is common for the mutual solubility of a pair of liquids to increase with temperature until misc...
The inevitable presence of water in high pressure-high temperature reservoirs leads to a number of n...
Liquid—vapor equilibrium phase compositions for the binary system normal hydrogen—helium have been d...
This paper presents vapor-liquid equilibrium data for the system hydrogen—benzene—cyclohexane— n -he...
Experiments were performed to study the phase behavior of gas condensate hydrocarbons at ...
The gas-liquid solubility of hydrogen in methanol, ethanol, 1-propanol, and 1-butanol at pressures i...
Owing to the highly supercritical nature of hydrogen in hydrogen-hydrocarbon systems, it is difficul...
Monte Carlo simulations were used to calculate water- methane and water- ethane phase equilibria ove...