| 731 - 736 |
Removal of hydrophilic compounds from water with organic polymers - Part II: Adsorption behavior of industrial wastewater
Frimmel FH, Assenmacher M, Kumke MU, Specht C, Abbt-Braun G, Grabe G |
| 737 - 741 |
Liquid-liquid equilibrium for the system n-heptane plus o-xylene plus triethylene glycol from 293.1 to 323.1 K
Darwish NA |
| 743 - 751 |
A one dimensional model for the prediction of extraction yields in a two phases modified twin-screw extruder
Prat L, Guiraud P, Rigal L, Gourdon C |
| 753 - 760 |
Two- and three-phase oxidation of ferrous sulfate to ferric sulfate - from intrinsic kinetics to diffusion-affected industrial kinetics
Ronnholm MR, Warna J, Salmi T |
| 761 - 764 |
Minimum fluidization velocities for gas-solid 2D beds
Caicedo GR, Ruiz MG, Marques JJP, Soler JG |
| 765 - 769 |
A method of predicting effective solvent extraction parameters for recycling of used lubricating oils
Elbashir NO, Al-Zahrani SM, Mutalib MIA, Abasaeed AE |
| 771 - 783 |
Flow phenomena in the exit zone of a circulating fluidized bed
Lackermeier U, Werther J |
| 785 - 792 |
Removal of hydrogen sulfide by clinoptilolite in a fixed bed adsorber
Yasyerli S, Ar I, Dogu G, Dogu T |
| 793 - 798 |
Effect of dissolved inorganic salts on the isothermal vapor-liquid equilibrium of the propionic acid-water mixture
Banat F, Al-Asheh S, Simandl J |
