• ExampleLaminar-1 Blending of Non-Newtonian liquid. Power. Circulation. Mixing time
• Example Turbulent-1. Power. Shear. Mixing time
• Example Turbulent-2. Heat Transfer. Initial Data and Calculation
• Example Turbulent-3. Liquid-solid mixing (suspending)
• Example Turbulent-4. Batch reactor scaling-up
• ExampleTurbulent-5. Crystalizer. Scaling-up
• Example Turbulent-7. Liquid-Liquid Mixing
• Example Turbulent-8.New features of Turbulent 2K7
• Example Turbulent-9.Nitration
• Example Turbulent2K7-1.Calculation of Main Hydrodynamic Parameters
• Example Turbulent2K7-2.Liquid-Solid Mixing
• Example Turbulent2K7-3.Scaling-up in Liquid-Liquid Extraction
• Example Turbulent2K7-4.Dissolution of Solid Particles
• Example Turbulent2K7-5.Heat Transfer Process in a Semibatch Reactor with Heat Consumption
• Example Turbulent2K7-6.Second Order Exothermal Reaction in Batch Reactor
• Example Turbulent2K7-7.Production of Propylene Glycole
• Example Turbulent2K7-8.Mechanical Calculations of Shafts
• Example Turbulent2K7-9.Evaluation of process duration in Gas-Liquid Reactor

Dow Chemicals Co. Dr. Victor Atiemo-Obeng

Emily Moore, Research Engineer, Xerox Research Centre of Canada

Dr. Roberto Bagatin, Enichem, Italy

Harbinder S Pordal, Ph.D.,Stress Engineering Services, OH,USA

Prof. F. Recasens, University of Barcelona, Spain

US Army, Eileen Heider, Project Engineer

Moshe Bentolila, Chemagis, Israel

CEPmagazine.org - a publication of the American Institute of Chemical Engineering, June 2003, Lead Story Fluids/Solids Handling, Optimizing Crystallizer Scaleup, by Wayne Genck, Ph.D

Lawrence H. Block, Ph.D., Professor of Pharmaceutics, Duquesne University, Pittsburgh, PA, USA

Kenneth Neeld, Solutia, USA

Unilever, Italy

Buchi AG, Switzerland

Degussa Company, Mr. Markus Doerner