729 - 731 |
Initial tests to detect quantitatively the coke loading of reforming catalysts by a contactless microwave method Muller N, Reiss S, Fremerey P, Jess A, Moos R |
732 - 740 |
Macro- and micromixing in a novel sonochemical reactor using high frequency ultrasound Parvizian F, Rahimi M, Faryadi M |
741 - 746 |
Particle distribution model of gibbsite precipitation process in alumina production Zhang JY, Li YQ, Zhang XH, Zhou JM |
747 - 756 |
A novel process for the synthesis of unsaturated polyester Shah M, Zondervan E, Oudshoorn ML, de Haan AB |
757 - 765 |
Optimization of protein encapsulation in PLGA nanoparticles Feczko T, Toth J, Dosa G, Gyenis J |
766 - 772 |
Process intensification with a hybrid system: A tubular packed bed bioreactor with immobilized activated sludge culture coupled with membrane filtration Dizge N, Tansel B, Sizirici B |
773 - 779 |
Simultaneous removal of gaseous pollutants with a novel swirl wet scrubber Pourmohammadbagher A, Jamshidi E, Ale-Ebrahim H, Dabir B, Mehrabani-Zeinabad M |
780 - 789 |
Negative pressure cavitation accelerated processing for extraction of main bioactive flavonoids from Radix Scutellariae Dong LL, Fu YJ, Zu YG, Li J, Li XJ, Efferth T |
790 - 798 |
Investigations on heat transfer and hydrodynamics under pyrolysis conditions of a pilot-plant draft tube conical spouted bed reactor Makibar J, Fernandez-Akarregi AR, Alava I, Cueva F, Lopez G, Olazar M |
799 - 809 |
On the efficiency of turbulent mixing in rotating stirrers Trivellato F |
810 - 814 |
Preparation of nanoparticles with a semi-batch gas-liquid membrane contactor Jia ZQ, Chang Q, Mamat A |
815 - 821 |
Process optimization of diafiltration with time-dependent water adding for albumin production Paulen R, Fikar M, Kovacs Z, Czermak P |
822 - 827 |
Extraction in microreactors: Intensification by adding an inert gas phase Assmann N, von Rohr PR |
828 - 835 |
Removal of fine particles by heterogeneous condensation in the double-alkali desulfurization process Bao JJ, Yang LJ, Sun WD, Geng JF, Yan JP, Shen XL |
836 - 845 |
Experimental study of gas-dynamically induced nanoparticle synthesis by use of adapted sampling probes Goertz V, Korp D, Al-Hasan N, Giglmaier M, Nirschl H |
846 - 853 |
Influence of process conditions on the mean size of PLGA nanoparticles Feczko T, Toth J, Dosa G, Gyenis J |
854 - 858 |
Elongated gas bubble dissolution under a turbulent liquid flow Valiorgue P, El Hajem M, Vassilev A, Botton V, Ben Hadid H |
859 - 868 |
Motion of a large object in a bubbling fluidized bed with a rotating distributor Soria-Verdugo A, Garcia-Hernando N, Almendros-Ibanez JA, Ruiz-Rivas U |
869 - 876 |
Short-channel structured reactor: Experiments versus previous theoretical design Kolodziej A, Lojewska J, Ochonska J, Lojewski T |
877 - 884 |
Single and two-phase pressure drop in serpentine mini-channels Donaldson AA, Kirpalani DM, Macchi A |
885 - 891 |
Effect of mixture composition, nanoparticle density and sound intensity on mixing quality of nanopowders Ammendola P, Chirone R, Raganati F |