| 165 - 186 |
Heat transfer in intermittent air-water flows - Part I Horizontal tube
Hetsroni G, Hu BG, Yi JH, Mosyak A, Yarin LP, Ziskind G |
| 189 - 210 |
Heat transfer in intermittent air-water flows - Part II - Upward inclined tube
Hetsroni G, Yi JH, Hu BG, Mosyak A, Yarin LP, Ziskind G |
| 213 - 223 |
Turbulent fluid and particle interaction in the boundary layer for cross flow over a tube
Fan JR, Zhang XY, Jin J, Zheng YQ, Cen KF |
| 225 - 242 |
Flow of concentrated non-Newtonian slurries : 1. Friction losses in laminar, turbulent and transition flow through straight pipe
Turian RM, Ma TW, Hsu FLG, Sung DJ |
| 243 - 269 |
Flow of concentrated non-Newtonian slurries : 2. Friction losses in bends, fittings, valves and Venturi meters
Turian RM, Ma TW, Hsu FLG, Sung MDJ, Plackmann GW |
| 271 - 281 |
A numerical model of Taylor bubbles rising through stagnant liquids in vertical tubes
Bugg JD, Mack K, Rezkallah KS |
| 283 - 293 |
The effect of gravity on the deposition of micron-sized particles on smooth surfaces
Yiantsios SG, Karabelas AJ |
| 295 - 315 |
On the dynamics of a two-phase, nonevaporating swirling jet
Park TW, Katta VR, Aggarwal SK |
| 319 - 334 |
Calculation of dryout and post-dryout heat transfer for tube geometry
Hoyer N |
| 335 - 345 |
Improved eddy interaction models with random length and time scales
Graham DI |
| 347 - 353 |
An experimental approach for the determination of development length in particulate flows
Carpinlioglu MO, Gundogdu MY |
