2561 - 2581 |
Obtainment of high-fructose solutions from cashew (Anacardium occidentale) apple juice by simulated moving-bed chromatography Azevedo DCS, Rodrigues A |
2583 - 2599 |
Modeling of mass transfer controlled adsorption rate based on the Langmuir adsorption isotherm Mondal K, Lalvani SB |
2601 - 2617 |
Biosorption of lead(II), nickel(II), and copper(II) on Rhizopus arrhizus from binary and ternary metal mixtures Sag Y, Kaya A, Kutsal T |
2619 - 2637 |
Low-frequency ultrasound to improve dead-end ultrafiltration performance Simon A, Gondrexon N, Taha S, Cabon J, Dorange G |
2639 - 2650 |
Particle collection efficiency of different impactor designs Tsai CJ, Lin TY |
2651 - 2662 |
Recovery of iron values from iron ore slimes by selective magnetic coating Prakash S, Das B, Mohapatra BK |
2663 - 2677 |
Flotation preconcentration of cobalt and nickel by lead(II) hexamethylenedithiocarbamate Pavlovska G, Cundeva K, Stafilov T |
2679 - 2705 |
Energy consumption and its reduction in the hydrocyclone separation process. III. Effect of the structure of flow field on energy consumption and energy saving principles Chu LY, Qin JJ, Chen WM, Lee XZ |
2707 - 2724 |
Mass transfer resistance analysis of L-tryptophan extraction in an emulsion liquid membrane system Liu XR, Liu DS |
2725 - 2743 |
Fractional separation and physicochemical characterization of polysaccharides from poplar chips Sun RC, Fang JM, Tomkinson J |
2745 - 2763 |
Isolation of rock rose essential oil using supercritical CO2 extraction Rincon J, De Lucas A, Garcia I |
2765 - 2781 |
Equilibrium-staged separations: A bibliography update (1999) Ray MS |