LEADER 01055nam0-22003011i-450- 001 990000145260403321 005 20030724164903.0 035 $a000014526 035 $aFED01000014526 035 $a(Aleph)000014526FED01 035 $a000014526 100 $a20020821d--------km-y0itay50------ba 101 0 $aita 105 $ay-------001yy 200 1 $a<>problema agronomico-meccanico della lavorazione del terreno$fF. Giordano, E. De Cillis, G.D. Mayer 210 $aMilano$cIstituto sperimentale di meccanica agraria$d1923 215 $a29 p.$cill.$d32 cm 300 $aEstr. da: Atti dell'Istituto sperimentale di meccanica, 1923. In testa al front.: Istituto sperimentale di meccanica 700 1$aGiordano,$bF.$0333840 702 1$aDe Cillis,$bEmanuele 702 1$aMayer,$bGiovan Domenico 801 0$aIT$bUNINA$gRICA$2UNIMARC 901 $aBK 912 $a990000145260403321 952 $a13 MISC 708 07$b5841$fFINBC 959 $aFINBC 996 $aProblema agronomico-meccanico della lavorazione del terreno$9113169 997 $aUNINA LEADER 05617nam 2200697 450 001 9910808123303321 005 20200520144314.0 010 $a1-5231-1062-7 010 $a1-118-51019-4 010 $a1-118-51013-5 010 $a1-118-51009-7 035 $a(CKB)2670000000355901 035 $a(EBL)1175202 035 $a(OCoLC)841908822 035 $a(SSID)ssj0000873421 035 $a(PQKBManifestationID)11957768 035 $a(PQKBTitleCode)TC0000873421 035 $a(PQKBWorkID)10878010 035 $a(PQKB)10090340 035 $a(MiAaPQ)EBC1175202 035 $a(Au-PeEL)EBL1175202 035 $a(CaPaEBR)ebr11099342 035 $a(PPN)223548367 035 $a(EXLCZ)992670000000355901 100 $a20160415h20132013 uy 0 101 0 $aeng 135 $aurcnu|||||||| 181 $ctxt 182 $cc 183 $acr 200 10$aDistillation design and control using Aspen simulation /$fWilliam L. Luyben 205 $aSecond edition. 210 1$aHoboken, New Jersey :$cAlChE :$cWiley,$d2013. 210 4$dİ2013 215 $a1 online resource (742 p.) 300 $aDescription based upon print version of record. 311 $a1-118-41143-9 320 $aIncludes bibliographical references and index. 327 $aCover; Title Page; Copyright; Dedication; Preface to the Second Edition; Preface to the First Edition; Chapter 1: Fundamentals of Vapor-Liquid-Equilibrium (VLE); 1.1 Vapor Pressure; 1.2 Binary VLE Phase Diagrams; 1.3 Physical Property Methods; 1.4 Relative Volatility; 1.5 Bubble Point Calculations; 1.6 Ternary Diagrams; 1.7 VLE Nonideality; 1.8 Residue Curves for Ternary Systems; 1.9 Distillation Boundaries; 1.10 Conclusions; Reference; Chapter 2: Analysis of Distillation Columns; 2.1 Design Degrees of Freedom; 2.2 Binary Mccabe-Thiele Method; 2.3 Approximate Multicomponent Methods 327 $a2.4 Conclusions Chapter 3: Setting Up a Steady-State Simulation; 3.1 Configuring a New Simulation; 3.2 Specifying Chemical Components and Physical Properties; 3.3 Specifying Stream Properties; 3.4 Specifying Parameters of Equipment; 3.5 Running the Simulation; 3.6 Using Design Spec/Vary Function; 3.7 Finding the Optimum Feed Tray and Minimum Conditions; 3.8 Column Sizing; 3.9 Conceptual Design; 3.10 Conclusions; Chapter 4: Distillation Economic Optimization; 4.1 Heuristic Optimization; 4.2 Economic Basis; 4.3 Results; 4.4 Operating Optimization; 4.5 Optimum Pressure for Vacuum Columns 327 $a4.6 Conclusions Chapter 5: More Complex Distillation Systems; 5.1 Extractive Distillation; 5.2 Ethanol Dehydration; 5.3 Pressure-Swing Azeotropic Distillation; 5.4 Heat-Integrated Columns; 5.5 Conclusions; Chapter 6: Steady-State Calculations for Control Structure Selection; 6.1 Control Structure Alternatives; 6.2 Feed Composition Sensitivity Analysis (ZSA); 6.3 Temperature Control Tray Selection; 6.4 Conclusions; Reference; Chapter 7: Converting From Steady-State to Dynamic Simulation; 7.1 Equipment Sizing; 7.2 Exporting to Aspen Dynamics; 7.3 Opening the Dynamic Simulation in Aspen Dynamics 327 $a7.4 Installing Basic Controllers 7.5 Installing Temperature and Composition Controllers; 7.6 Performance Evaluation; 7.7 Conclusions; Chapter 8: Control of More Complex Columns; 8.1 Extractive Distillation Process; 8.2 Columns with Partial Condensers; 8.3 Control of Heat-Integrated Distillation Columns; 8.4 Control of Azeotropic Columns/Decanter System; 8.5 Unusual Control Structure; 8.6 Conclusions; References; Chapter 9: Reactive Distillation; 9.1 Introduction; 9.2 Types of Reactive Distillation Systems; 9.3 Tame Process Basics; 9.4 Tame Reaction Kinetics and Vle 327 $a9.5 Plantwide Control Structure 9.6 Conclusions; References; Chapter 10: Control of Sidestream Columns; 10.1 Liquid Sidestream Column; 10.2 Vapor Sidestream Column; 10.3 Liquid Sidestream Column with Stripper; 10.4 Vapor Sidestream Column with Rectifier; 10.5 Sidestream Purge Column; 10.6 Conclusions; Chapter 11: Control of Petroleum Fractionators; 11.1 Petroleum Fractions; 11.2 Characterization Crude Oil; 11.3 Steady-State Design of Preflash Column; 11.4 Control of Preflash Column; 11.5 Steady-State Design of Pipestill; 11.6 Control of Pipestill; 11.7 Conclusions; References 327 $aChapter 12: Divided-Wall (Petlyuk) Columns 330 $aThe new edition of this book greatly updates and expands the previous edition. It boasts new chapters on the divided wall column and carbon dioxide capture from stack gas, revises the design and control of distillation systems, and explains the use of dynamic simulation to study safety issues in the event of operating failures. Using Aspen Plus to develop rigorous simulations of single distillation columns and sequences of columns, the book considers the economics of capital investment and energy costs to create an optimal system for separation methods in the chemical and petroleum industries. 606 $aDistillation apparatus$xDesign and construction 606 $aChemical process control$xSimulation methods 606 $aPetroleum$xRefining 615 0$aDistillation apparatus$xDesign and construction. 615 0$aChemical process control$xSimulation methods. 615 0$aPetroleum$xRefining. 676 $a660/.28425 700 $aLuyben$b William L.$016520 712 02$aAmerican Institute of Chemical Engineers. 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910808123303321 996 $aDistillation Design and Control Using Aspen SImulation$9716264 997 $aUNINA