02403oam 22006974a 450 991045501280332120210915045640.00-8018-7523-4(CKB)111056486619362(EBL)3318072(OCoLC)923190978(SSID)ssj0000235499(PQKBManifestationID)11176152(PQKBTitleCode)TC0000235499(PQKBWorkID)10247479(PQKB)10093585(SSID)ssj0000474938(PQKBManifestationID)12174609(PQKBTitleCode)TC0000474938(PQKBWorkID)10455315(PQKB)11044295(MiAaPQ)EBC3318072(OCoLC)1017993446(MdBmJHUP)muse82420(Au-PeEL)EBL3318072(CaPaEBR)ebr10021521(EXLCZ)9911105648661936220001220d2002 uy 0engur|n|---|||||txtccrReligion and ViolencePhilosophical Perspectives from Kant to Derrida /Hent de VriesLondon :Johns Hopkins University Press,2002.©2002.1 online resource (472 p.)TRAITEMENT SOMMAIRE.Titre de l'ecran-titre (visionne le 8 août 2011).0-8018-6768-1 0-8018-6767-3 Includes bibliographical references and index.Contents; Preface and Acknowledgments; Abbreviations; Introduction:Horror Religiosus; Chapter 1 - State, Academy, Censorship; Chapter 2 - Violence and Testimony; Chapter 3 - Anti-Babel; Chapter 4 - Hospitable Thought; Bibliography; IndexViolenceReligious aspectsfast(OCoLC)fst01167248Philosophy and religionfast(OCoLC)fst01060826Philosophy and religionViolenceReligious aspectsLivres electroniques.Electronic books. ViolenceReligious aspects.Philosophy and religion.Philosophy and religion.ViolenceReligious aspects.291.5/697Vries Hent de733667MdBmJHUPMdBmJHUPBOOK9910455012803321Religion and violence2181000UNINA05378nam 2200685Ia 450 991083037070332120170809170535.01-282-11265-197866121126520-470-37774-70-470-37779-8(CKB)1000000000719508(EBL)427670(OCoLC)476269836(SSID)ssj0000232883(PQKBManifestationID)11220057(PQKBTitleCode)TC0000232883(PQKBWorkID)10219420(PQKB)10202414(MiAaPQ)EBC427670(PPN)203761731(EXLCZ)99100000000071950820080215d2008 uy 0engur|n|---|||||txtccrReactive distillation design and control[electronic resource] /William L. Luyben, Cheng-Ching YuHoboken, NJ John Wileyc20081 online resource (598 p.)Includes index.0-470-22612-9 REACTIVE DISTILLATION DESIGN AND CONTROL; CONTENTS; PREFACE; 1 INTRODUCTION; 1.1 History; 1.2 Basics of Reactive Distillation; 1.3 Neat Operation Versus Excess Reactant; 1.4 Limitations; 1.4.1 Temperature Mismatch; 1.4.2 Unfavorable Volatilities; 1.4.3 Slow Reaction Rates; 1.4.4 Other Restrictions; 1.5 Scope; 1.6 Computational Methods; 1.6.1 Matlab Programs for Steady-State Design; 1.6.2 Aspen Simulations; 1.7 Reference Materials; PART I STEADY-STATE DESIGN OF IDEAL QUATERNARY SYSTEM; 2 PARAMETER EFFECTS; 2.1 Effect of Holdup on Reactive Trays; 2.2 Effect of Number of Reactive Trays2.3 Effect of Pressure2.4 Effect of Chemical Equilibrium Constant; 2.5 Effect of Relative Volatilities; 2.5.1 Constant Relative Volatilities; 2.5.2 Temperature-Dependent Relative Volatilities; 2.6 Effect of Number of Stripping and Rectifying Trays; 2.7 Effect of Reactant Feed Location; 2.7.1 Reactant A Feed Location (N(FA)); 2.7.2 Reactant B Feed Location (N(FB)); 2.8 Conclusion; 3 ECONOMIC COMPARISON OF REACTIVE DISTILLATION WITH A CONVENTIONAL PROCESS; 3.1 Conventional Multiunit Process; 3.1.1 Assumptions and Specifications; 3.1.2 Steady-State Design Procedure3.1.3 Sizing and Economic Equations3.2 Reactive Distillation Design; 3.2.1 Assumptions and Specifications; 3.2.2 Steady-State Design Procedure; 3.3 Results for Different Chemical Equilibrium Constants; 3.3.1 Conventional Process; 3.3.2 Reactive Distillation Process; 3.3.3 Comparisons; 3.4 Results for Temperature-Dependent Relative Volatilities; 3.4.1 Relative Volatilities; 3.4.2 Optimum Steady-State Designs; 3.4.3 Real Chemical Systems; 3.5 Conclusion; 4 NEAT OPERATION VERSUS USING EXCESS REACTANT; 4.1 Introduction; 4.2 Neat Reactive Column; 4.3 Two-Column System with Excess B4.3.1 20% Excess B Case4.3.2 10% Excess B Case; 4.4 Two-Column System with 20% Excess of A; 4.5 Economic Comparison; 4.6 Conclusion; PART II STEADY-STATE DESIGN OF OTHER IDEAL SYSTEMS; 5 TERNARY REACTIVE DISTILLATION SYSTEMS; 5.1 Ternary System Without Inerts; 5.1.1 Column Configuration; 5.1.2 Chemistry and Phase Equilibrium Parameters; 5.1.3 Design Parameters and Procedure; 5.1.4 Effect of Pressure; 5.1.5 Holdup on Reactive Trays; 5.1.6 Number of Reactive Trays; 5.1.7 Number of Stripping Trays; 5.2 Ternary System With Inerts; 5.2.1 Column Configuration5.2.2 Chemistry and Phase Equilibrium Parameters5.2.3 Design Parameters and Procedure; 5.2.4 Effect of Pressure; 5.2.5 Control Tray Composition; 5.2.6 Reactive Tray Holdup; 5.2.7 Effect of Reflux; 5.2.8 Chemical Equilibrium Constant; 5.2.9 Feed Composition; 5.2.10 Number of Reactive Trays; 5.2.11 Number of Rectifying and Stripping Trays; 5.3 Conclusion; 6 TERNARY DECOMPOSITION REACTION; 6.1 Ternary Decomposition Reaction: Intermediate-Boiling Reactant; 6.1.1 Column Configuration; 6.1.2 Chemistry and Phase Equilibrium Parameters; 6.1.3 Design Parameters and Procedure6.1.4 Holdup on Reactive TraysAfter an overview of the fundamentals, limitations, and scope of reactive distillation, this book uses rigorous models for steady-state design and dynamic analysis of different types of reactive distillation columns and quantitatively compares the economics of reactive distillation columns with conventional multi-unit processes. It goes beyond traditional steady-state design that primarily considers the capital investment and energy costs when analyzing the control structure and the dynamic robustness of disturbances, and discusses how to maximize the economic and environmental benefits of reaDistillation apparatusDesign and constructionChemical process controlDistillationReactivity (Chemistry)Distillation apparatusDesign and construction.Chemical process control.Distillation.Reactivity (Chemistry)660660.28425660/.28425Luyben William L16520Yu Cheng-Ching1956-1679498MiAaPQMiAaPQMiAaPQBOOK9910830370703321Reactive distillation design and control4047770UNINA