| 1 |
Development and test of a new Knudsen effusion apparatus for the measurement of low vapour pressures
Fonseca JMS, Pfohl O, Dohrn R
Journal of Chemical Thermodynamics, 43(12), 1942, 2011 |
| 2 |
Phase equilibria and diffusion coefficients in the poly(dimethylsiloxane) plus n-pentane system
Kruger KM, Pfohl O, Dohrn R, Sadowski G
Fluid Phase Equilibria, 241(1-2), 138, 2006 |
| 3 |
Provision of thermodynamic properties of polymer systems for industrial applications
Pfohl O, Dohrn R
Fluid Phase Equilibria, 217(2), 189, 2004 |
| 4 |
Thermophysical properties - Industrial directions
Dohrn R, Pfohl O
Fluid Phase Equilibria, 194, 15, 2002 |
| 5 |
Measurement and calculation of phase equilibria in the system n-pentane plus poly(dimethylsiloxane) at 308.15-423.15 K
Pfohl O, Riebesell C, Dohrn R
Fluid Phase Equilibria, 202(2), 289, 2002 |
| 6 |
About "Prediction of phase equilibria for CO2-C2H5OH-H2O system using the SAFT equation of state" by Zhang et al. [Fluid Phase Equilib. 169 (2000) 1-18]
Pfohl O, Budich M
Fluid Phase Equilibria, 189(1-2), 179, 2001 |
| 7 |
Phase equilibria in systems containing o-cresol, p-cresol, carbon dioxide, and ethanol at 323.15-473.15 K and 10-35 MPa
Pfohl O, Pagel A, Brunner G
Fluid Phase Equilibria, 157(1), 53, 1999 |
| 8 |
Evaluation of an improved volume translation for the prediction of hydrocarbon volumetric properties
Pfohl O
Fluid Phase Equilibria, 163(1), 157, 1999 |
| 9 |
1. Comparison of 12 equations of state with respect to gas-extraction processes : Reproduction of pure-component properties when enforcing the correct critical temperature and pressure
Pfohl O, Giese T, Dohrn R, Brunner G
Industrial & Engineering Chemistry Research, 37(8), 2957, 1998 |
| 10 |
2. Use of BACK to modify SAFT in order to enable density and phase equilibrium calculations connected to gas-extraction processes
Pfohl O, Brunner G
Industrial & Engineering Chemistry Research, 37(8), 2966, 1998 |
