LEADER 05493nam 2200649Ia 450 001 9910144003403321 005 20230721030222.0 010 $a1-280-92156-0 010 $a9786610921560 010 $a3-527-61060-X 010 $a3-527-61059-6 035 $a(CKB)1000000000376063 035 $a(EBL)482104 035 $a(OCoLC)173134526 035 $a(SSID)ssj0000204013 035 $a(PQKBManifestationID)11199590 035 $a(PQKBTitleCode)TC0000204013 035 $a(PQKBWorkID)10174818 035 $a(PQKB)10085331 035 $a(MiAaPQ)EBC482104 035 $a(EXLCZ)991000000000376063 100 $a20061204d2007 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 00$aModeling of process intensification /$fedited by Frerich Johannes Keil 210 $aWeinheim $cWiley-VCH ;$aChichester $cJohn Wiley [distributor]$d2007 215 $a1 online resource (424 p.) 300 $aDescription based upon print version of record. 311 $a3-527-31143-2 320 $aIncludes bibliographical references and index. 327 $aModeling of Process Intensification; Contents; Preface; List of Contributors; 1 Modeling of Process Intensification - An Introduction and Overview; 2 Process Intensification - An Industrial Point of View; 2.1 Introduction; 2.1.1 Remarks on the Term Process Intensification; 2.1.2 Management Aspects; 2.2 Microreaction Technology; 2.2.1 Principal Features; 2.2.2 Catalytic Wall Reactors; 2.3 Simulation; 2.3.1 Introduction; 2.3.2 Molecular Simulations; 2.3.2.1 Quantum-chemical Calculations; 2.3.2.2 COSMO-RS Calculations; 2.3.2.3 Molecular-dynamics Calculations 327 $a2.3.3 Monte Carlo Simulations in Project Valuation under Risk3 Modeling and Simulation of Microreactors; 3.1 Introduction; 3.2 Flow Distributions; 3.2.1 Straight Microchannels; 3.2.2 Periodic and Curved Channel Geometries; 3.2.3 Multichannel Flow Domains; 3.3 Heat Transfer; 3.3.1 Straight Microchannels; 3.3.2 Periodic and Curved Channel Geometries; 3.3.3 Multichannel Flow Domains; 3.3.4 Micro Heat Exchangers; 3.4 Mass Transfer and Mixing; 3.4.1 Simple Mixing Channels; 3.4.2 Chaotic Micromixers; 3.4.3 Multilamination Micromixers; 3.4.4 Hydrodynamic Dispersion; 3.5 Chemical Kinetics 327 $a3.5.1 Numerical Methods for Reacting Flows3.5.2 Reacting Channel Flows; 3.5.3 Heat-exchanger Reactors; 3.6 Conclusions and Outlook; 4 Modeling and Simulation of Unsteady-state-operated Trickle-flow Reactors; 4.1 Introduction; 4.2 Modeling; 4.3 Reactor Model; 4.4 Simulation; 4.5 Conclusion; 5 Packed-bed Membrane Reactors; 5.1 Introduction; 5.1.1 The PBMR Principle; 5.1.2 Case Study; 5.1.3 Porous Membranes; 5.1.4 Outline; 5.2 One-dimensional Modeling of Packed-bed Membrane Reactors; 5.2.1 One-dimensional Pseudohomogeneous Model 327 $a5.2.2 Cofeed (FBR) vs. Distributed Dosing of Reactants (PBMR) - Nonreactive Conditions5.2.3 Comparison between FBR and PBMR - Reactive Conditions; 5.2.4 Nonisothermal Operation; 5.3 Two-dimensional Modeling of Packed-bed Membrane Reactors; 5.3.1 Two-dimensional Model of PBMR - The Momentum-balance Equation; 5.3.2 Two-dimensional Model of PBMR - The Mass-balance Equation; 5.3.3 Two-dimensional Model of PBMR - The Energy-balance Equation; 5.3.4 Boundary Conditions; 5.3.5 Numerical Solution of the Two-dimensional Model; 5.3.6 Velocity Field in a Packed-bed Membrane Reactor 327 $a5.3.7 The Influence of Membrane Permeability on the Boundary Conditions5.3.8 Effect of Porosity Profile; 5.3.9 Effect of Radial Mass-transport Limitations; 5.3.10 Comparison of the ?(r)- and ?(w)-model Concepts - Temperature Profiles in a PBMR; 5.4 Three-dimensional Modeling of a Packed-bed Membrane Reactor; 5.4.1 Introduction to the Large-scale Simulation Methods in Fluid Mechanics and Mass Transport; 5.4.2 Pressure and Velocity Field (Varying the Flow Distribution) - Comparison between FBR and PBMR; 5.4.3 Advective-diffusive Mass Transport in PBMR; 5.5 Summary and Conclusion 327 $a6 The Focused Action of Surface Tension versus the Brute Force of Turbulence - Scaleable Microchannel-based Process Intensification using Monoliths 330 $aCombining the knowledge involved in process engineering and process modeling, this is the first book to cover all modeling methods applicable to process intensification. Both the editors and authors are renowned experts from industry and academia in the various fields of process modeling and integrated chemical processes. Following an introduction to the topic, the book goes on to look at equipment and operational methods, monolithic catalysis, HEX, micro- and reverse flow reactors, catalytic and reactive distillation, the simulated-moving bed and vibration bubble column as well as ultraso 606 $aChemical process control 606 $aChemical process control$xMathematical models 606 $aChemical process control$xSimulation methods 615 0$aChemical process control. 615 0$aChemical process control$xMathematical models. 615 0$aChemical process control$xSimulation methods. 676 $a660.15118 676 $a660.2815 701 $aKeil$b Frerich$f1947-$023088 712 02$aWiley Online Library (Servicio en línea) 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910144003403321 996 $aModeling of process intensification$92201236 997 $aUNINA