00874cam0-22003011i-450-99000592213040332119980601000592213FED01000592213(Aleph)000592213FED0100059221319980601d1920----km-y0itay50------baitaITy-------001yy<<I >>Reati di falsola natura giuridica dei reati di falso di fronte alla dottrina e al Codice penale italianoMarcello FinziMilanoFratelli Bocca1920XXXIII, 581 p.25 cm34520itaFinzi,Marcello224577ITUNINARICAUNIMARCBK990005922130403321MASSARI D 853972FGBCXII D 618094FGBCFGBCReati di falso562123UNINA01119nam0 2200277 i 450 SUN006577320180724094036.66988-435-3295-220081002d1990 |0itac50 baitaIT|||| |||||Alberto Viania cura di Pier Carlo SantiniMilano : Electa[1990]332 p. : ill. ; 26 cmCatalogo della Mostra tenuta a Mantova nel 1990. - Nell'occhietto: Centro internazionale d'arte e di cultura di Palazzo Te.MilanoSUNL000284Santini, Pier CarloSUNV052322Viani, AlbertoSUNV052323ElectaSUNV008644650ITSOL20181109RICASUN0065773UFFICIO DI BIBLIOTECA DEL DIPARTIMENTO DI LETTERE E BENI CULTURALI07 CONS Pa Viani 1978 07 2097 UFFICIO DI BIBLIOTECA DEL DIPARTIMENTO DI LETTERE E BENI CULTURALIIT-CE01032097CONS Pa Viani 1978caAlberto Viani608897UNICAMPANIA05353nam 2200637Ia 450 991102047170332120200520144314.01-281-75883-397866117588373-527-61601-23-527-61600-4(CKB)1000000000376229(EBL)481340(SSID)ssj0000120415(PQKBManifestationID)11131870(PQKBTitleCode)TC0000120415(PQKBWorkID)10081040(PQKB)10586564(MiAaPQ)EBC481340(PPN)153160667(OCoLC)212133965(EXLCZ)99100000000037622919950427d2000 uy 0engur|n|---|||||txtccrChemical engineering dynamics an introduction to modelling and computer simulation /John Ingham ... [et al.]2nd completely rev. ed.Weinheim ;New York VCHc20001 online resource (670 p.)Description based upon print version of record.3-527-28577-6 Includes bibliographical references and index.Chemical Engineering Dynamics; Preface; Organisation of the Book; Acknowledgements; Table of Contents; Nomenclature for Chapters 1 to 4; 1 Basic Concepts; 1.1 Modelling Fundamentals; 1.1.1 Chemical Engineering Modelling; 1.1.2 General Aspects of the Modelling Approach; 1.1.3 General Modelling Procedure; 1.2 Formulation of Dynamic Models; 1.2.1 Material Balance Equations; 1.2.2 Balancing Procedures; 1.2.2.1 Case A . Continuous Stirred-Tank Reactor; 1.2.2.2 Case B . Tubular Reactor; 1.2.2.3 Case C . Coffee Percolator; 1.2.3 Total Material Balances; 1.2.3.1 Case A . Tank Drainage1.2.4 Component Balances1.2.4.1 Case A . Waste Holding Tank; 1.2.4.2 Case B . Extraction from a Solid by a Solvent; 1.2.5 Energy Balancing; 1.2.5.1 Case A . Continuous Heating in an Agitated Tank; 1.2.5.2 Case B . Heating in a Filling Tank; 1.2.5.3 Case C . Parallel Reaction in a Semi-Continuous Reactor with Large Temperature Changes; 1.2.6 Momentum Balances; 1.2.7 Dimensionless Model Equations; 1.2.7.1 Case A . Continuous Stirred-Tank Reactor (CSTR); 1.2.7.2 Case B . Gas-Liquid Mass Transfer to a Continuous Tank Reactor with Chemical Reaction; 1.3 Chemical Kinetics1.3.1 Rate of Chemical Reaction1.3.2 Reaction Rate Constant; 1.3.3 Heats of Reaction; 1.3.4 Chemical Equilibrium and Temperature; 1.3.5 Yield, Conversion and Selectivity; 1.4 Microbial Growth Kinetics; 1.5 Mass Transfer Theory; 1.5.1 Stagewise and Differential Mass Transfer Contacting; 1.5.2 Phase Equilibria; 1.5.3 Interphase Mass Transfer; 2 Process Dynamics Fundamentals; 2.1 Signal and Process Dynamics; 2.1.1 Measurement and Process Response; 2.1.1.1 First-Order Response to an Input Step-Change Disturbance; 2.1.1.2 Case A . Concentration Response of a Continuous Flow, Stirred Tank2.1.1.3 Case B . Concentration Response in a Continuous Stirred Tank with Chemical Reaction2.1.1.4 Case C . Response of a Temperature Measuring Element; 2.1.1.5 Case D . Measurement Lag for Concentration in a Batch Reactor; 2.1.2 Higher-order Responses; 2.1.2.1 Case A . Multiple Tanks in Series; 2.1.2.2 Case B . Response of a Second-Order Temperature Measuring Element; 2.1.3 Pure Time Delay; 2.1.4 Transfer Function Representation; 2.2 Time Constants; 2.2.1 Common Time Constants; 2.2.1.1 Flow Phenomena; 2.2.1.2 Diffusion and Dispersion; 2.2.1.3 Chemical Reaction; 2.2.1.4 Mass Transfer2.2.1.5 Heat Transfer2.2.2 Application of Time Constants; 2.3 Fundamentals of Automatic Control; 2.3.1 Basic Feedback Control; 2.3.2 Types of Controller Action; 2.3.2.1 On/Off Control; 2.3.2.2 Proportional-Integral-Derivative (PID) Control; 2.3.2.3 Case A . Operation of a Proportional Temperature Controller; 2.3.3 Controller Tuning; 2.3.3.1 Trial and Error Method; 2.3.3.2 Ziegler-Nichols Method; 2.3.3.3 Cohen-Coon Controller Settings; 2.3.3.4 Ultimate Gain Method; 2.3.3.5 Time Integral Criteria; 2.3.4 Advanced Control Strategies; 2.3.4.1 Cascade Control; 2.3.4.2 Feedforward Control2.3.4.3 Adaptive ControlIn this book, the reader is guided through the complex study of dynamic chemical engineering systems by the unique combination of a simplified presentation of the fundamental theory (Part 1) and direct hands-on computer experimentation with the provision of 85 accompanying computer-based simulation examples (Part 2) supplied on diskette.The ISIM digital simulation language is very simple to use and its powerful interactive nature enables the readers to create their own simulations, based on their own specific problems. This powerful dynamic ISIM software is ready to run on any DOS persChemical engineeringComputer simulationChemical processesData processingChemical engineeringComputer simulation.Chemical processesData processing.660.28660.28155362Ingham JohnDr.21598MiAaPQMiAaPQMiAaPQBOOK9911020471703321Chemical engineering dynamics2041672UNINA