| 1 |
A Novel Theory for Predicting Critical Constants and the alpha Function for Pure Polymers
Twu CH
Industrial & Engineering Chemistry Research, 49(22), 11801, 2010 |
| 2 |
Rigorously Universal Methodology of Volume Translation for Cubic Equations of State
Twu CH, Chan HS
Industrial & Engineering Chemistry Research, 48(12), 5901, 2009 |
| 3 |
Methodology for predicting water content in supercritical gas vapor and gas solubility in aqueous phase for natural gas process
Twu CH, Watanasiri S, Tassone V
Industrial & Engineering Chemistry Research, 46(22), 7253, 2007 |
| 4 |
Advanced equation of state method for modeling TEG-water for glycol gas dehydration
Twu CH, Tassone V, Sim WD, Watanasiri S
Fluid Phase Equilibria, 228, 213, 2005 |
| 5 |
Accurately predict the VLE of thiol-hydrocarbon mixtures
Twu CH, Tassone V, Sim WD
Chemical Engineering Progress, 100(9), 39, 2004 |
| 6 |
New solid equation of state combining excess energy mixing rule for solid-liquid equilibria
Twu CH, Tassone V, Sim WD
AIChE Journal, 49(11), 2957, 2003 |
| 7 |
Getting a handle on advanced cubic equations of state
Twu CH, Sim WD, Tassone V
Chemical Engineering Progress, 98(11), 58, 2002 |
| 8 |
A versatile liquid activity model for SRK, PR and a new cubic equation-of-state TST
Twu CH, Sim WD, Tassone V
Fluid Phase Equilibria, 194, 385, 2002 |
| 9 |
An extension of CEOS/A(E) zero-pressure mixing rules for an optimum two-parameter cubic equation of state
Twu CH, Sim WD, Tassone V
Industrial & Engineering Chemistry Research, 41(5), 931, 2002 |
| 10 |
Liquid activity coefficient model for CEOS/A(E) mixing rules
Twu CH, Sim WD, Tassone V
Fluid Phase Equilibria, 183-184, 65, 2001 |
