| 1 |
Gibbs energy approach for aqueous processes with HF, HNO3, and CO2-CaCO3
Salminen J, Kobylin P, Liukkonen S, Chiavone-Filho O
AIChE Journal, 50(8), 1942, 2004 |
| 2 |
Vapor liquid equilibrium for the binary systems 2-methylpentane+2-butanol at 329.2 K and n-hexane+2-butanol at 329.2 and 363.2 K with a static apparatus
Uusi-Kyyny P, Pokki JP, Laakkonen M, Aittamaa J, Liukkonen S
Fluid Phase Equilibria, 201(2), 343, 2002 |
| 3 |
Vapor-liquid equilibrium for the 2-methylpentane+2-methyl-2-propanol and+2-butanol systems at 329 K
Pokki JP, Uusi-Kyyny P, Aittamaa J, Liukkonen S
Journal of Chemical and Engineering Data, 47(2), 371, 2002 |
| 4 |
Combination of overall reaction rate with Gibbs energy minimization
Koukkari P, Laukkanen I, Liukkonen S
Fluid Phase Equilibria, 136(1-2), 345, 1997 |
| 5 |
An Improved Correlation for Compressed Liquid Densities of Hydrocarbons .1. Pure Compounds
Aalto M, Keskinen KI, Aittamaa J, Liukkonen S
Fluid Phase Equilibria, 114(1-2), 1, 1996 |
| 6 |
An Improved Correlation for Compressed Liquid Densities of Hydrocarbons .2. Mixtures
Aalto M, Keskinen KI, Aittamaa J, Liukkonen S
Fluid Phase Equilibria, 114(1-2), 21, 1996 |
| 7 |
Bubble Point Pressures and Densities for the Binary-Systems of Propane with Triacontane, Hexatriacontane, Tetracontane, Pentacontane, and Squalane at 353-373 K and 4.00-7.00 MPa
Aalto M, Liukkonen S
Journal of Chemical and Engineering Data, 41(1), 79, 1996 |
