LEADER 01520nam 2200481 a 450 001 9910690030503321 005 20021115124013.0 035 $a(CKB)5470000002334960 035 $a(OCoLC)31422033 035 9 $aocm31422033 035 $a(OCoLC)995470000002334960 035 $a(EXLCZ)995470000002334960 100 $a19941108d1994 ua 0 101 0 $aeng 181 $ctxt$2rdacontent 182 $cn$2rdamedia 183 $anc$2rdacarrier 200 10$aHerbicide tolerance/resistance in plants $eApril 1991 - March 1994 /$fRaymond Dobert 210 1$aBeltsville, Md. :$cNational Agricultural Library,$d[1994] 215 $a113 pages ;$d28 cm 225 1 $aQuick bibliography series,$x1052-5378 ;$vQB 94-60 300 $a"342 citations in English from AGRICOLA." 300 $a"September 1994." 300 $a"Updates QB 91-104." 300 $aIncludes indexes. 300 $aShipping list no.: 94-0337-P. 517 $aHerbicide tolerance/resistance in plants 606 $aHerbicide resistance$vBibliography 606 $aPlants$xHerbicide tolerance$vBibliography 608 $aBibliographies.$2lcgft 615 0$aHerbicide resistance 615 0$aPlants$xHerbicide tolerance 700 $aDobert$b Raymond$01382214 712 02$aNational Agricultural Library (U.S.) 801 0$bDGPO 801 1$bDLC 801 2$bGPO 801 2$bOCLCQ 801 2$bGPO 906 $aBOOK 912 $a9910690030503321 996 $aHerbicide tolerance$93425432 997 $aUNINA LEADER 05371nam 2200685Ia 450 001 9911019744303321 005 20200520144314.0 010 $a9781283927581 010 $a1283927586 010 $a9781118001646 010 $a1118001648 010 $a9781118001653 010 $a1118001656 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(Perlego)1012207 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 /$fWilliam L. Luyben 210 $aHoboken, N.J. $cJohn Wiley$dc2011 215 $a1 online resource (342 p.) 300 $aDescription based upon print version of record. 311 08$a9781118001639 311 08$a111800163X 311 08$a9780470927083 311 08$a0470927089 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 $a9911019744303321 996 $aPrinciples and case studies of simultaneous design$91080280 997 $aUNINA