658 - 658 |
3D Analysis of Heat Transfer Intensification by Re-Entrance Flow Pin-Fins Microstructures with a Highly Thermal-Conductive Plate (vol 34, pg 379, 2011) Wang Q, Hessel V, Rebrov EV, Werner B |
663 - 672 |
Applying Model Predictive Control to Dividing Wall Columns Buck C, Hiller C, Fieg G |
673 - 687 |
Integration of Ultrafiltration Unit Operations in Biotechnology Process Design Grote F, Frohlich H, Strube J |
688 - 698 |
Integrated Simulated Moving Bed Processes for Production of Single Enantiomers Palacios JG, Kaspereit M, Kienle A |
699 - 706 |
Oxidation of Phenol by Microbubble-Assisted Microelectrolysis Ren YZ, Wu ZL, Ondruschka B, Braeutigam P, Franke M, Nehring H, Hampel U |
707 - 717 |
Experimental Apparatus for Studying Heat Transfer in Externally Heated Rotary Kilns Thammavong P, Debacq M, Vitu S, Dupoizat M |
718 - 726 |
Application of Cross-Flow Microfiltration for Purifying Solvent Naphtha with Ceramic Membranes Zeng JX, Zheng LF, Sun XH, He QC |
727 - 736 |
Aging and Thermal Stability of the Mixed Product of the Ether-Soluble Fraction of Bio-Oil and Bio-Diesel Jiang XX, Zhong ZP, Ellis N, Wang Q |
737 - 745 |
Improved Tank in Series Reactor Model for Tubular Solid Oxide Fuel Cell Stacks Danilov VA, Vijay P, Tade MO |
746 - 750 |
Implementation and Operation of a Dividing-Wall Distillation Column Barroso-Munoz FO, Hernandez S, Segovia-Hernandez JG, Hernandez-Escoto H, Rico-Ramirez V, Chavez RH |
751 - 759 |
Prediction of the Profit Function for Industrial 2-Keto-L-Gulonic Acid Cultivation Cui L, Xu YY, Jia Q, Wu HT, Yuan JQ |
760 - 766 |
Hydrodynamic Behaviors in Gas-Solid Two-Phase Magnetic Fluidized Beds 1. Experimental Results Represented by a Dimensionless Number Li H, Cao CQ, Zhao YA |
767 - 774 |
Unsteady Mixing Characteristics in a Vessel with Forward-Reverse Rotating Impeller Woziwodzki S |
775 - 783 |
Removal of Chromium and Organic Pollutants from Industrial Chrome Tanning Effluents by Electrocoagulation Golder AK, Samanta AN, Ray S |
784 - 790 |
Estimation of Coalescence Parameters in an Agitated Extraction Column Using a Hybrid Algorithm Kabouche A, Meniai AH, Hasseine A |
791 - 796 |
Monitoring the Ammonia Loading of Zeolite-Based Ammonia SCR Catalysts by a Microwave Method Reiss S, Schonauer D, Hagen G, Fischerauer G, Moos R |
797 - 802 |
Ion-Exchange Equilibria of Nitrates on a Strongly Basic Resin Chabani M, Akhrib K, Ouaissa YA, Amrane A, Bensmaili A |
803 - 808 |
Hydrodesulfurization-Supported Catalysts: Effect of the Preparation Method Moradi P, Parvari M |
809 - 816 |
Net Present Value Analysis of Modular Chemical Production Plants Lier S, Grunewald M |
817 - 822 |
Optimization of Methanol Yield from a Lurgi Reactor Chen L, Jiang QZ, Song ZZ, Posarac D |
823 - 830 |
Kinetic Model of Gas-Liquid-Liquid Reactive Extraction for Production of Hydrogen Peroxide Lu SX, Wang L, Wang YQ, Mi ZT |
831 - 836 |
Mesoporous Glass Membranes as Model Systems to Study Gas Diffusion through Porous Media Stoltenberg D, Seidel-Morgenstern A, Enke D |
837 - 840 |
In Situ Microscopy for Online Monitoring of Enzyme Carriers and Two-Phase Processes Prediger A, Bluma A, Hopfner T, Lindner P, Beutel S, Scheper T, Muller JJ, Hilterhaus L, Liese A |