2685 - 2697 |
Film model approximation for particle-diffusion-controlled multicomponent ion exchange Carta G, Lewus RK |
2699 - 2721 |
Numerical simulation of elution chromatography for separation of H-2-HD-D-2 mixtures using a palladium particle bed Fukada S |
2723 - 2739 |
Comparison of novel and patented silica-polyamine composite materials as aqueous heavy metal ion recovery materials Beatty ST, Fischer RJ, Rosenberg E, Pang D |
2741 - 2760 |
Ammonia removal from wastewaters using natural Australian zeolite. II. Pilot-scale study using continuous packed column process Cooney EL, Booker NA, Shallcross DC, Stevens GW |
2761 - 2779 |
Nickel biosorption from aqueous systems: Studies on single and multimetal equilibria, kinetics, and recovery Suhasini IP, Sriram G, Asolekar SR, Sureshkumar GK |
2781 - 2792 |
Flux enhancement with powdered activated carbon addition in the membrane anaerobic bioreactor Park H, Choo KH, Lee CH |
2793 - 2802 |
Immobilized metal affinity membrane separation: Characteristics of two materials of differing preparation chemistries Crawford J, Ramakrishnan S, Periera P, Gardner S, Coleman M, Beitle R |
2803 - 2815 |
Fouling studies of a pervaporation membrane with commercial fermentation media and fermentation broth of hyper-butanol-producing Clostridium beijerinckii BA101 Qureshi N, Blaschek HP |
2817 - 2836 |
Theoretical assessment of dilute acetone removal from aqueous streams by membrane distillation Abu Al-Rub F, Banat FA, Shannag M |
2837 - 2851 |
Analysis of mass transfer performance in an air stripping tower Chung TW, Lai CH, Wu HD |
2853 - 2863 |
Mass transfer model for supercritical fluid extraction tests Al-Jabari ME, Weber ME |
2865 - 2886 |
Extraction of Cs-137 and Sr-90 from alkaline solutions with high NaNO3 content with tetrahexyldicarbollide Rais J, Selucky P, Sistkova NV, Alexova J |
2887 - 2903 |
Effects of solvent recycling on radiolytic degradation of 30% tributyl phosphate-n-dodecane-HNO3 system Tripathi SC, Sumathi S, Ramanujam A |
2905 - 2922 |
Recovery of theophylline in effluent with 2-ethylhexanol extraction process Hu X |