LEADER 05228nam 2200613Ia 450 001 9910830583403321 005 20230725032244.0 010 $a1-283-92758-6 010 $a1-118-00164-8 010 $a1-118-00165-6 035 $a(CKB)2670000000128107 035 $a(EBL)697663 035 $a(OCoLC)757511529 035 $a(SSID)ssj0000597344 035 $a(PQKBManifestationID)11378995 035 $a(PQKBTitleCode)TC0000597344 035 $a(PQKBWorkID)10578101 035 $a(PQKB)11451332 035 $a(MiAaPQ)EBC697663 035 $a(EXLCZ)992670000000128107 100 $a20100922d2011 uy 0 101 0 $aeng 135 $aur|n|---||||| 181 $ctxt 182 $cc 183 $acr 200 10$aPrinciples and case studies of simultaneous design$b[electronic resource] /$fWilliam L. Luyben 210 $aHoboken, N.J. $cJohn Wiley$dc2011 215 $a1 online resource (342 p.) 300 $aDescription based upon print version of record. 311 $a1-118-00163-X 311 $a0-470-92708-9 320 $aIncludes bibliographical references and index. 327 $aPRINCIPLES ANDCASE STUDIES OFSIMULTANEOUS DESIGN; PREFACE; 1 INTRODUCTION; 1.1 Overview; 1.2 History; 1.3 Books; 1.4 Tools; Reference Textbooks; 2 PRINCIPLES OF REACTOR DESIGN AND CONTROL; 2.1 Background; 2.2 Principles Derived from Chemistry; 2.2.1 Heat of Reaction; 2.2.2 Reversible and Irreversible Reactions; 2.2.3 Multiple Reactions; 2.3 Principles Derived from Phase of Reaction; 2.4 Determining Kinetic Parameters; 2.4.1 Thermodynamic Constraints; 2.4.2 Kinetic Parameters from Plant Data; 2.5 Principles of Reactor Heat Exchange; 2.5.1 Continuous Stirred-Tank Reactors 327 $a2.5.2 Tubular Reactors2.5.3 Feed-Effluent Heat Exchangers; 2.6 Heuristic Design of Reactor/Separation Processes; 2.6.1 Introduction; 2.6.2 Process Studied; 2.6.3 Economic Optimization; 2.6.4 Other Cases; 2.6.5 Real Example; 2.7 Conclusion; References; 3 PRINCIPLES OF DISTILLATION DESIGN AND CONTROL; 3.1 Principles of Economic Distillation Design; 3.1.1 Operating Pressure; 3.1.2 Heuristic Optimization; 3.1.3 Rigorous Optimization; 3.1.4 Feed Preheating and Intermediate Reboilers and Condensers; 3.1.5 Heat Integration; 3.2 Principles of Distillation Control; 3.2.1 Single-End Control 327 $a3.2.2 Dual-End Control3.2.3 Alternative Control Structures; 3.3 Conclusion; References; 4 PRINCIPLES OF PLANTWIDE CONTROL; 4.1 History; 4.2 Effects of Recycle; 4.2.1 Time Constants of Integrated Plant with Recycle; 4.2.2 Recycle Snowball Effect; 4.3 Management of Fresh Feed Streams; 4.3.1 Fundamentals; 4.3.2 Process with Two Recycles and Two Fresh Feeds; 4.4 Conclusion; 5 ECONOMIC BASIS; 5.1 Level of Accuracy; 5.2 Sizing Equipment; 5.2.1 Vessels; 5.2.2 Heat Exchangers; 5.2.3 Compressors; 5.2.4 Pumps, Valves, and Piping; 5.3 Equipment Capital Cost; 5.3.1 Vessels (diameter and length in meters) 327 $a5.3.2 Heat Exchangers (area in square meters)5.3.3 Compressors (work in horsepower); 5.4 Energy Costs; 5.5 Chemical Costs; References; 6 DESIGN AND CONTROL OF THE ACETONE PROCESS VIA DEHYDROGENATION OF ISOPROPANOL; 6.1 Process Description; 6.1.1 Reaction Kinetics; 6.1.2 Phase Equilibrium; 6.2 Turton Flowsheet; 6.2.1 Vaporizer; 6.2.2 Reactor; 6.2.3 Heat Exchangers, Flash Tank, and Absorber; 6.2.4 Acetone Column C1; 6.2.5 Water Column C2; 6.3 Revised Flowsheet; 6.3.1 Effect of Absorber Pressure; 6.3.2 Effect of Water Solvent and Absorber Stages; 6.3.3 Effect of Reactor Size 327 $a6.3.4 Optimum Distillation Design6.4 Economic Comparison; 6.5 Plantwide Control; 6.5.1 Control Structure; 6.5.2 Column Control Structure Selection; 6.5.3 Dynamic Performance Results; 6.6 Conclusion; References; 7 DESIGN AND CONTROL OF AN AUTO-REFRIGERATED ALKYLATION PROCESS; 7.1 Introduction; 7.2 Process Description; 7.2.1 Reaction Kinetics; 7.2.2 Phase Equilibrium; 7.2.3 Flowsheet; 7.2.4 Design Optimization Variables; 7.3 Design of Distillation Columns; 7.3.1 Depropanizer; 7.3.2 Deisobutanizer; 7.4 Economic Optimization of Entire Process; 7.4.1 Flowsheet Convergence; 7.4.2 Yield 327 $a7.4.3 Effect of Reactor Size 330 $aThere are many comprehensive design books, but none of them provide a significant number of detailed economic design examples of typically complex industrial processes. Most of the current design books cover a wide variety of topics associated with process design. In addition to discussing flowsheet development and equipment design, these textbooks go into a lot of detail on engineering economics and other many peripheral subjects such as written and oral skills, ethics, ""green"" engineering and product design. This book presents general process design principles in a concise readable form th 606 $aChemical engineering 606 $aEngineering design 615 0$aChemical engineering. 615 0$aEngineering design. 676 $a660.2812 676 $a660/.2812 700 $aLuyben$b William L$016520 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910830583403321 996 $aPrinciples and case studies of simultaneous design$91080280 997 $aUNINA LEADER 03754nam 22006615 450 001 9910299976903321 005 20250609110059.0 010 $a3-0348-0736-8 024 7 $a10.1007/978-3-0348-0736-4 035 $a(CKB)3710000000212205 035 $a(Springer)9783034807364 035 $a(MH)014131694-2 035 $a(SSID)ssj0001296458 035 $a(PQKBManifestationID)11721671 035 $a(PQKBTitleCode)TC0001296458 035 $a(PQKBWorkID)11347690 035 $a(PQKB)11201961 035 $a(DE-He213)978-3-0348-0736-4 035 $a(MiAaPQ)EBC6314607 035 $a(MiAaPQ)EBC5586448 035 $a(Au-PeEL)EBL5586448 035 $a(OCoLC)1066184980 035 $a(PPN)179927000 035 $a(MiAaPQ)EBC1783840 035 $a(EXLCZ)993710000000212205 100 $a20140714d2014 u| 0 101 0 $aeng 135 $aurnn|008mamaa 181 $ctxt$2rdacontent 182 $cc$2rdamedia 183 $acr$2rdacarrier 200 10$aDispersive Equations and Nonlinear Waves $eGeneralized Korteweg?de Vries, Nonlinear Schrödinger, Wave and Schrödinger Maps /$fby Herbert Koch, Daniel Tataru, Monica Vi?an 205 $a1st ed. 2014. 210 1$aBasel :$cSpringer Basel :$cImprint: Birkhäuser,$d2014. 215 $a1 online resource (XII, 312 p. 1 illus.)$conline resource 225 1 $aOberwolfach Seminars,$x1661-237X ;$v45 300 $aBibliographic Level Mode of Issuance: Monograph 311 08$a3-0348-0735-X 320 $aIncludes bibliographical references (pages [309]-312). 330 $aThe first part of the book provides an introduction to key tools and techniques in dispersive equations: Strichartz estimates, bilinear estimates, modulation and adapted function spaces, with an application to the generalized Korteweg-de Vries equation and the Kadomtsev-Petviashvili equation. The energy-critical nonlinear Schrödinger equation, global solutions to the defocusing problem, and scattering are the focus of the second part. Using this concrete example, it walks the reader through the induction on energy technique, which has become the essential methodology for tackling large data critical problems. This includes refined/inverse Strichartz estimates, the existence and almost periodicity of minimal blow up solutions, and the development of long-time Strichartz inequalities. The third part describes wave and Schrödinger maps. Starting by building heuristics about multilinear estimates, it provides a detailed outline of this very active area of geometric/dispersive PDE. It focuses on concepts and ideas and should provide graduate students with a stepping stone to this exciting direction of research. 410 0$aOberwolfach Seminars,$x1661-237X ;$v45 606 $aDifferential equations, Partial 606 $aPartial Differential Equations$3https://scigraph.springernature.com/ontologies/product-market-codes/M12155 615 0$aDifferential equations, Partial. 615 14$aPartial Differential Equations. 676 $a515.355 676 $a530.124 700 $aKoch$b Herbert$4aut$4http://id.loc.gov/vocabulary/relators/aut$036792 702 $aTataru$b Daniel$4aut$4http://id.loc.gov/vocabulary/relators/aut 702 $aVi?an$b Monica$4aut$4http://id.loc.gov/vocabulary/relators/aut 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910299976903321 996 $aDispersive Equations and Nonlinear Waves$92541504 997 $aUNINA 999 $aThis Record contains information from the Harvard Library Bibliographic Dataset, which is provided by the Harvard Library under its Bibliographic Dataset Use Terms and includes data made available by, among others the Library of Congress