| 189 - 197 |
The operating performance of stirred column reactor
Sun JZ, Wang DC, Pan ZR |
| 198 - 212 |
A G(E) equation of state mixing rule for vapor-liquid equilibria
Qu YX, Wang WC, Lee YY, Chung KY, Lee YW |
| 213 - 221 |
The performance of EOS models in the prediction of vapor-liquid equilibria in asymmetric natural gas mixtures
Wang LS, Gardeler H, Gmehling J |
| 222 - 232 |
Modeling of the relationship between pore size distribution and thickness of ceramic MF membrane
Dong JH, Wang P, Xu NP, Shi J, Lin JYS |
| 233 - 238 |
A general equation for calculating the ＇true＇ height of transfer unit in extraction columns
Luo GS, Li HB, Fei WY, Wang JD |
| 239 - 247 |
The solubility of styrene from polystyrene in supercritical CO2
Jiang CY, Pan QM, Pan ZR |
| 248 - 256 |
Kinetic correlation for the hindered diffusion of proteins in a porous packing column
Yu ZX, He ZM |
| 257 - 263 |
A statistical thermodynamic model of vapor-liquid interfacial tension for liquid mixtures at high pressure
Li ZB, Li JF, Li YG |
| 264 - 270 |
A novel constitutive equation for viscoelastic-thixotropic fluids and its application in the characterization of blood hysteresis loop
Fang B, Jiang TQ |
| 271 - 276 |
Approximate expressions to evaluate the performance in butene-1 purification units
Bressa SP, Ardiaca NO, Martinez OM, Barreto GF |
| 277 - 282 |
Using process energy integration technology in the energy-saving retrofit of large-scale complex chemical process system
Li HQ, Yao PJ |
