1 |
Predicting Calorimetric Properties Using the Original and the Modified Simplified-Perturbed-Hard-Chain Theory Equations of State Chunangad KS, Row KH, Robinson RL, Gasem KA Fluid Phase Equilibria, 131(1-2), 119, 1997 |
2 |
Determination of Infinite Dilution Activity-Coefficients for Organic-Aqueous Systems Using a Dilute Vapor-Liquid-Equilibrium Method Bader MS, Gasem KA Chemical Engineering Communications, 140, 41, 1996 |
3 |
Solubilities of Hydrogen in Aromatic-Hydrocarbons from 323 to 433 K and Pressures to 21.7 MPa Park J, Robinson RL, Gasem KA Journal of Chemical and Engineering Data, 41(1), 70, 1996 |
4 |
Modified SPHCT Equation of State for Improved Predictions of Equilibrium and Volumetric Properties of Pure Fluids Shaver RD, Robinson RL, Gasem KA Fluid Phase Equilibria, 112(2), 223, 1995 |
5 |
Solution Algorithms and Parameter Sensitivity Analysis for the SPHCT Equation of State Shaver RD, Robinson RL, Gasem KA Fluid Phase Equilibria, 113(1-2), 61, 1995 |
6 |
Solubilities of Carbon-Monoxide in Heavy Normal-Paraffins at Temperatures from 311-K to 423-K and Pressures to 10.2-MPa Srivatsan S, Yi XH, Robinson RL, Gasem KA Journal of Chemical and Engineering Data, 40(1), 237, 1995 |
7 |
Solubilities of Hydrogen in Heavy Normal-Paraffins at Temperatures from 323.2-K to 423.2-K and Pressures to 17.4-MPa Park J, Robinson RL, Gasem KA Journal of Chemical and Engineering Data, 40(1), 241, 1995 |
8 |
Solubilities of Carbon-Monoxide in Aromatic-Hydrocarbons at Temperatures from 323-K to 433-K and Pressures to 23.3-MPa Park J, Yi XH, Gasem KA, Robinson RL Journal of Chemical and Engineering Data, 40(1), 245, 1995 |
9 |
Predicting Gas-Adsorption Using 2-Dimensional Equations of State Zhou CH, Hall F, Gasem KA, Robinson RL Industrial & Engineering Chemistry Research, 33(5), 1280, 1994 |
10 |
Solubility of Methane in Benzene, Naphthalene, Phenanthrene, and Pyrene at Temperatures from 323 to 433-K and Pressures to 11.3 MPa Darwish NA, Gasem KA, Robinson RL Journal of Chemical and Engineering Data, 39(4), 781, 1994 |