International audienceThis work reports high-quality isothermal vapor-liquid equilibrium data for ethane + ethanethiol (or ethyl mercaptan) at 303 K, 323 K and 343 K and pressures up to 6.25 MPa. A sapphire-tube equilibrium cell with an online micro sampler and GC-TCD are employed to measure equilibrium phase concentrations at specific temperatures and pressures. Peng Robinson equation of state with classical alpha function is found adequate for data treatment and thermodynamic modelling
A modified version of an apparatus by Sage and Lacey for phase equilibrium measurements at elevated ...
International audienceIn this work, vapor-liquid equilibrium (VLE) measurements of propyl mercaptan ...
A total pressure apparatus has been developed to measure vapour-liquid equilibrium data on binary mi...
International audienceDesign of debutaniser in fractionation train in gas processing requires accura...
International audienceIsothermal vapor-liquid equilibrium data are presented for the ethane (R170) +...
International audienceNovel isothermal (p-x-y) vapor-liquid equilibrium data are reported for ethane...
We acknowledge the Scottish Funding Council for providing a travel grant to Dr Waheed Afzal under No...
International audienceIsothermal vapor−liquid equilibrium data for the perfluorobutane (R610) + etha...
International audienceIn this paper, new vapour-liquid equilibrium data of the (ethane + R1234ze(E))...
International audienceA static total pressure method was employed to determine the vapor pressures o...
In this work, new isothermal experimental data of vapor-liquid equilibrium of the isobutane and ethy...
International audienceIsothermal vapor-liquid equilibrium data are reported for ethylene + 1,1,2,3,3...
A study of vapour-liquid equilibria is presented together with current developments. The theory of v...
Vapor–liquid, liquid–liquid, and vapor–liquid–liquid equilibria of the binary system nitrogen + etha...
Isobaric vapor liquid equilibrium (VLE) data were measured for the systems ethanol + 2,4,4-trimethyl...
A modified version of an apparatus by Sage and Lacey for phase equilibrium measurements at elevated ...
International audienceIn this work, vapor-liquid equilibrium (VLE) measurements of propyl mercaptan ...
A total pressure apparatus has been developed to measure vapour-liquid equilibrium data on binary mi...
International audienceDesign of debutaniser in fractionation train in gas processing requires accura...
International audienceIsothermal vapor-liquid equilibrium data are presented for the ethane (R170) +...
International audienceNovel isothermal (p-x-y) vapor-liquid equilibrium data are reported for ethane...
We acknowledge the Scottish Funding Council for providing a travel grant to Dr Waheed Afzal under No...
International audienceIsothermal vapor−liquid equilibrium data for the perfluorobutane (R610) + etha...
International audienceIn this paper, new vapour-liquid equilibrium data of the (ethane + R1234ze(E))...
International audienceA static total pressure method was employed to determine the vapor pressures o...
In this work, new isothermal experimental data of vapor-liquid equilibrium of the isobutane and ethy...
International audienceIsothermal vapor-liquid equilibrium data are reported for ethylene + 1,1,2,3,3...
A study of vapour-liquid equilibria is presented together with current developments. The theory of v...
Vapor–liquid, liquid–liquid, and vapor–liquid–liquid equilibria of the binary system nitrogen + etha...
Isobaric vapor liquid equilibrium (VLE) data were measured for the systems ethanol + 2,4,4-trimethyl...
A modified version of an apparatus by Sage and Lacey for phase equilibrium measurements at elevated ...
International audienceIn this work, vapor-liquid equilibrium (VLE) measurements of propyl mercaptan ...
A total pressure apparatus has been developed to measure vapour-liquid equilibrium data on binary mi...