| 293 - 306 |
Selection of control structure and temperature location for two-product distillation columns
Hori ES, Skogestad S |
| 307 - 319 |
Heat and mass transfer in U-bend of a pneumatic conveying dryer
Hidayat M, Rasmuson A |
| 320 - 328 |
Direct-contact heat transfer coefficient for condensing vapour bubble in stagnant liquid pool
Kar S, Chen XD, Nelson MI |
| 329 - 343 |
Modelling of heat and mass transport phenomena and chemical reaction in underground coal gasification
Perkins G, Sahajwalla V |
| 344 - 356 |
Struvite crystallization in fed-batch pilot scale and description of solution chemistry of struvite
Ali MI |
| 357 - 364 |
A new experimental technique for determining local dispersion coefficient in displacement washing
Lindau J, Sedin P, Theliander H |
| 365 - 376 |
Technical evaluation of a reverse osmosis desalination plant in the Caribbean: A case study
Ramdhanie IC, Riverol C |
| 377 - 385 |
Experimental characterization of pressure drop in dry demisters at low and elevated pressures
Helsor T, Svendsen H |
| 386 - 394 |
Mass transfer from a plane surface immersed in a porous medium with a moving fluid
Delgado JMPQ |
| 395 - 405 |
Liquid/liquid viscous dispersions with a SMX static mixer
Fradette L, Tanguy P, Li HZ, Choplin L |
| 406 - 409 |
Control of polymorphs and crystal habit in crystallization of N-2-(1(S)-ethoxycarbonyl-3-phenylpropyl)-N-6-trifluoroacetyl-L-lysine
Ueda Y, Iida Y, Manabe H, Kitamura M |
