633 - 649 |
Microfiltration of protein precipitate from clarified yeast cell homogenate for the recovery of a soluble product Levesley JA, Seggianni M, Hoare M |
651 - 666 |
Determination of the working optimum parameters for an electrodialysis reversal pilot plant Valerdi-Perez R, Berna-Amoros LM, Ibanez-Mengual JA |
667 - 687 |
Purification of hydrogen by pressure swing adsorption Sircar S, Golden TC |
689 - 701 |
Adsorption of Ni2+ from aqueous solutions by pretreated biomass of marine macroalga Durvillaea potatorum Yu QM, Kaewsarn P |
703 - 713 |
Temperature effect on copper isotopes separation by electron-exchange reaction using anion-exchange chromatography Matin MA, Kim SH, Nomura M, Fujii Y |
715 - 727 |
Comparative analysis of different approaches for theoretical simulation of ultracentrifuge isotopic separation cascades Portoghese CCP, Rodrigues C |
729 - 741 |
A second-order time-accurate method for determination of concentration distribution of multicomponent mixtures in separation cascades Zeng S, Ying CT |
743 - 754 |
Thermodynamic modeling and experimental studies of dearomatization process from a complex petroleum fraction Vakili-Nezhaad GR, Modarress H, Mansoori GA |
755 - 765 |
Correlation for prediction of extraction characteristics for separation of weak acids-bases by liquid surfactant membrane Bhowal A, Datta S |
767 - 778 |
A lipophilic acyclic polyether dicarboxylic acid as Pb2+ carrier in polymer inclusion and bulk liquid membranes Lee SC, Lamb JD, Cho MH, Rhee CH, Kim JS |
779 - 784 |
A comparison between the picrate and inductively coupled plasma-atomic emission spectroscopy (ICP-AES) methods of metal assays in solution for calix[4]arene amides and amines as extractants Mohapatra P, Sriram S, Manchanda V, Badheka L |