231 - 239 |
Transport mechanism of sulfuric acid through an anion exchange membrane Lorrain Y, Pourcelly G, Gavach C |
241 - 251 |
A numerical model of steady-state permeate flux during cross-flow ultrafiltration Lee YH, Clark MM |
253 - 261 |
Electrokinetic characterization of polyethersulfone UF membranes Ricq L, Pierre A, Bayle S, Reggiani JC |
263 - 267 |
Ultrafiltration of agricultural waste waters with organic and inorganic membranes Reimann W, Yeo I |
269 - 275 |
Submarine and underground reverse osmosis schemes for energy-efficient seawater desalination Reali M, deGerloni M, Sampaolo A |
277 - 284 |
A simulation study to improve the performance of a solar humidification-dehumidification desalination unit constructed in Jordan Nawayseh NK, Farid MM, Omar AA, AlHallaj SM, Tamimi AR |
285 - 302 |
Energy consumption and costs with a multi-stage flashing (MSF) desalting system Darwish MA, Yousef FA, AlNajem NM |
303 - 313 |
Influence of specially modulated ultrasound on the water desalination process with ion-exchange hollow fibers Band M, Gutman M, Faerman V, Korngold E, Kost J, Plath PJ, Gontar V |
315 - 321 |
Alicante University, closed water cycle, reverse osmosis and water treatment plants Prats D, Chillon MF, Rubio M, Reverter JA |
323 - 332 |
Evaluation of SHMP and advanced scale inhibitors for control of CaSO4, SrSO4, and CaCO3 scales in RO desalination Butt FH, Rahman F, Baduruthamal U |