| 3353 - 3383 |
Hybrid processes: Design method for optimal coupling of chromatography and crystallization units
Strohlein G, Schulte M, Strube J |
| 3385 - 3407 |
Ion exchange resins as reversible acid gas absorbents
Quinn R |
| 3409 - 3430 |
Separation of phenylenediamines by selective solubilization and adsorption on ion-exchange resin
Kamble SP, Gaikar VG |
| 3431 - 3447 |
Selective separation of uranium containing glutamic acid molecular-imprinted polymeric microbeads
Say R, Erosz A, Denizli A |
| 3449 - 3458 |
Effect of PVP additive on porous polysulfone membrane formation by immersion precipitation method
Matsuyama H, Maki T, Teramoto M, Kobayashi K |
| 3459 - 3472 |
Ion exchange characteristics of palladium and ruthenium from a simulated radioactive liquid waste
Lee SH, Chung H |
| 3473 - 3491 |
Dehydration of industrial ketonic effluents by pervaporation. Comparative behavior of ceramic and polymeric membranes
Urtiaga AM, Casado C, Aragoza C, Ortiz I |
| 3493 - 3511 |
A high-duty horizontal dust-collector with a rotary baffle
Bryczkowski A, Smolka W |
| 3513 - 3534 |
The cementation of cadmium ion in aqueous solution by a zinc column test
Shen YS, Ku Y, Wu MH |
| 3535 - 3552 |
Mass transfer characteristics of bale-type catalytic distillation packings
Manduca E, Gonzalez JC, Elman H |
| 3553 - 3574 |
Separation of cobalt from a nickel-hydrometallurgical effluent using an emulsion liquid membrane
Fang JZ, Li MY, Xu ZH |
| 3575 - 3589 |
Separation of Te(IV) and Se(IV) by extraction with Cyanex 925
Mhaske AA, Dhadke PM |
| 3591 - 3607 |
Gold recovery by pH-switching process via cloud point extraction
Wongwailikhit K, Tasakorn P, Prasassarakich P, Aratono M |
| 3609 - 3624 |
Theobromine and caffeine recovery with solvent extraction
Hu X, Wan XJ, Bal RS, Yang HW |
