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1. |
Record Nr. |
UNISA996387229003316 |
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Autore |
Mocket Thomas <1602-1670?> |
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Titolo |
A vievv of the Solemn Leagve and Covenant [[electronic resource] ] : for reformation, defence of religion, the honour and happynesse of the King, and the peace, safety and union of the three kingdoms of England, Scotland, and Ireland, to be taken by all / by T. Mocket . |
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Pubbl/distr/stampa |
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London, : Printed for Christopher Meredith ..., 1644 |
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Descrizione fisica |
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Lingua di pubblicazione |
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Formato |
Materiale a stampa |
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Livello bibliografico |
Monografia |
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Note generali |
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Reproduction of original in Thomason Collection, British Library. |
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Sommario/riassunto |
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2. |
Record Nr. |
UNICASPUV0302420 |
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Autore |
Gell-Mann, Murray |
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Titolo |
Il quark e il giaguaro : avventure nel semplice e nel complesso / Murray Gell-Mann |
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Pubbl/distr/stampa |
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Torino, : Bollati Boringhieri, 1996 |
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Titolo uniforme |
The quark and the jaguar |
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ISBN |
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Descrizione fisica |
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Collana |
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Disciplina |
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Soggetti |
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Cosmologia |
Fisica - Teorie |
Sistemi complessi |
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Lingua di pubblicazione |
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Formato |
Materiale a stampa |
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Livello bibliografico |
Monografia |
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Note generali |
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3. |
Record Nr. |
UNINA9910789146403321 |
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Autore |
Tai Jacky |
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Titolo |
Brand zero : the complete branding guide for start-ups / / Jacky Tai |
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Pubbl/distr/stampa |
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Singapore : , : Marshall Cavendish Business, , [2014] |
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©2014 |
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ISBN |
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Descrizione fisica |
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1 online resource (213 p.) |
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Disciplina |
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Soggetti |
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Branding (Marketing) |
Brand name products - Management |
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Lingua di pubblicazione |
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Formato |
Materiale a stampa |
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Livello bibliografico |
Monografia |
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Note generali |
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Description based upon print version of record. |
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Nota di contenuto |
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Contents; Introduction; 1; 2; 3; 4; 5; 6; 7; 8; 9; 10; Final Word; About The Author |
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Sommario/riassunto |
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If you are thinking of starting up a business - whether online or in a pushcart or a small café - you need to look into your branding. (how does it work, anyway?), brace yourself...According to Jacky Tai, you should start your branding exercise as early as possible. Brand Zero distils the author's wealth of experience in grappling with branding strategies in the real world into a practical and easy-to-understand guide anyone. |
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4. |
Record Nr. |
UNINA9910830887803321 |
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Autore |
Liu Y. A. |
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Titolo |
Integrated Process Modeling, Advanced Control and Data Analytics for Optimizing Polyolefin Manufacturing / / Y. A. Liu and Niket Sharma |
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Pubbl/distr/stampa |
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Weinheim, Germany : , : WILEY-VCH GmbH, , [2023] |
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©2023 |
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ISBN |
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3-527-84383-3 |
3-527-84381-7 |
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Edizione |
[First edition.] |
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Descrizione fisica |
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1 online resource (865 pages) |
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Disciplina |
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Soggetti |
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Lingua di pubblicazione |
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Formato |
Materiale a stampa |
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Livello bibliografico |
Monografia |
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Nota di bibliografia |
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Includes bibliographical references and index. |
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Nota di contenuto |
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Cover -- Volume 1 -- Title Page -- Copyright -- Contents -- Foreword -- Preface -- Acknowledgment -- Copyright Notice -- About the Authors -- About the Companion Website -- Chapter 1 Introduction to Integrated Process Modeling, Advanced Control, and Data Analytics in Optimizing Polyolefin Manufacturing -- 1.1 Segment‐Based Modeling of Polymerization Processes: Component Characterization and Polymer Attributes -- 1.1.1 Component Types in Polymer Process Modeling -- 1.1.2 Concept of Moments and Some Basic Polymer Attributes -- 1.1.3 Stream Initialization and Basic Polymer Attributes -- 1.2 Workshop 1.1: Finding the Resulting Stream Attributes After Mixing Two Copolymer Streams -- 1.2.1 Objective -- 1.2.2 Problem Statement -- 1.2.3 Process Flowsheet -- 1.2.4 Unit System, Components, and Characterization of Copolymers -- 1.2.5 Property Method and Property Parameters for Components -- 1.2.6 Specifications of Streams and Blocks -- 1.3 Workshop 1.2: A Simplified Simulation Model for a Slurry HDPE Process and the Workflow for Developing a Polymer Process Simulation Model -- 1.3.1 Objective -- 1.3.2 Step 1: Problem Setup -- 1.3.3 Step 2: Component Specifications -- 1.3.4 Step 3: Property Method -- 1.3.5 Step 4: Property Parameters - Obtaining Values from Databanks and Estimating Missing Parameters -- 1.3.6 Step 5: Verification of the Accuracy of the Selected Property Method by Comparing Predicted Pure‐Component Property Values with Report |
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Experimental Data -- 1.3.7 Step 6: Regress Component Liquid Density Data and Binary Vapor-Liquid Equilibrium (TPXY) Data to Estimate Missing Pure‐component and Binary Interaction Parameters of Selected Property Method and Verify Predicted VLE Results with Experimental Data -- 1.3.8 Step 7: Develop Correlations for Polymer Product Quality Indices, Such as Density and Melt Index (Melt Flow Rate) Based on Plant Data. |
1.3.9 Step 8: Define the Polymerization Reactions and Enter the Initial Reaction Rate Constants -- 1.3.10 Step 9: Draw the Open‐Loop Process Flowsheet and Enter the Inputs for Streams and Blocks -- 1.3.11 Step 10: Run the Initial Open‐loop Process Simulation and Check if the Simulation Results Are Reasonable -- 1.3.12 Step 11: Close the Recycled Loops, Finalize a Converged Closed‐loop Steady‐state Simulation Model, and Investigate Applications to Improving Process Operations and Identifying Operating Conditions for New Product Design -- 1.3.13 Step 12: Convert the Steady‐state Simulation Model in Aspen Plus to a Dynamic Simulation Model in Aspen Plus Dynamics -- Add Appropriate Controllers -- and Investigate Process Operability, Control, and Grade Changes -- 1.4 Industrial and Potential Applications of Integrated Process Modeling, Advanced Control, and Data Analytics to Optimizing Polyolefin Manufacturing -- 1.4.1 Industrial and Potential Applications of Process Modeling to Optimizing Polyolefin Manufacturing -- 1.4.2 Industrial and Potential Applications of Advanced Process Control to Optimizing Polyolefin Manufacturing -- 1.4.3 Industrial and Potential Applications of Data Analytics to Optimizing Polyolefin Manufacturing -- 1.4.4 Hybrid Modeling: Integrated Applications of Process Modeling, Advanced Control, and Data Analytics to Optimizing Polyolefin Manufacturing -- References -- Chapter 2 Selection of Property Methods and Estimation of Physical Properties for Polymer Process Modeling -- 2.1 Property Methods and Thermophysical Parameter Requirements for Process Simulation -- 2.2 Polymer Activity Coefficient Models (ACM): Polymer Nonrandom Two‐liquid (POLYNRTL) Model -- 2.2.1 Vapor-Liquid Equilibrium for an Ideal Vapor Phase and a Nonideal Liquid Phase. |
2.2.2 General Vapor-Liquid Equilibrium Relationships Based on Fugacity Coefficient and Liquid‐phase Activity Coefficient -- 2.2.3 Segment‐based Mole Fraction Versus Species‐based Mole Fraction -- 2.2.4 POLYNRTL: Polymer Nonrandom Two‐liquid Activity Coefficient Model -- 2.2.5 Concept of Henry Components for Vapor-Liquid Equilibrium for a Vapor Phase and a Nonideal Liquid Phase Involving Supercritical Components -- 2.3 Workshop 2.1. Estimating POLYNRTL Binary Parameters Using UNIFAC -- 2.3.1 Objective -- 2.3.2 Estimating POLYNRTL Binary Parameters Using UNIFAC for Polystyrene Manufacturing -- 2.4 Prediction of Polymer Physical Properties by Van Krevelen Functional Group Method -- 2.5 Workshop 2.2. Estimating the Physical Properties of a Copolymer Using the Van Krevelen Group Contribution Method -- 2.5.1 Objective -- 2.5.2 Draw the Process Flowsheet and Specify the Unit Set and Global Options -- 2.5.3 Define Components, Segments, and Polymer and Characterize Their Structures -- 2.5.4 Choosing Property Method and Entering or Estimating Property Parameters -- 2.5.5 Specifications of Feed Stream and Flash Block -- 2.5.6 Creating Property Sets -- 2.5.7 Defining Property Analysis Run to Create Property Tables -- 2.6 Polymer Sanchez-Lacombe Equation of State (POLYSL) -- 2.7 Workshop 2.3. Estimating Property Parameters Using Data Regression Tool -- 2.7.1 Objective -- 2.7.2 Defining a DRS Run -- 2.7.3 Specifying a Unit Set and Global Options -- 2.7.4 Defining Components, Segments, Oligomers, and Polymer -- 2.7.5 Choose Property Method and Enter Known Property Parameters from Aspen |
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Enterprise Databanks -- 2.7.6 Enter Experimental Data for Data Regression, Run the Regression, and Examine the Results -- 2.7.7 Specifying a Regression Run and the Parameters to be Regressed -- 2.7.8 Running the Regression Case and Examining the Results. |
2.8 Polymer Perturbed‐chain Statistical Fluid Theory (POLYPCSF) Equation of State -- 2.9 Workshop 2.4. Regression of Property Parameters for POLYPCSF EOS -- 2.9.1 Objective and Data Sources -- 2.9.2 Regression of Pure Component Parameters for POLYPCSF EOS -- 2.10 Correlation of Polymer Product Quality Indices and Structure-Property Correlations -- 2.10.1 Polyolefin Product Quality Indices -- 2.10.2 Empirical Correlations of Polymer Product Quality Targets -- 2.10.3 Estimation of Apparent Newtonian Viscosity from MI‐MWW Measurement -- References -- Chapter 3 Reactor Modeling, Convergence Tips, and Data‐Fit Tool -- 3.1 Kinetic or Rate‐Based Reactors -- 3.2 Continuous Stirred‐Tank Reactor Model (RCSTR) -- 3.2.1 RCSTR Configurations -- 3.2.2 RCSTR Specifications -- 3.3 Plug‐Flow Reactor Model (RPLUG) -- 3.3.1 RPLUG Configurations -- 3.3.2 RPLUG Specifications -- 3.4 Batch Reactor Model (RBATCH) -- 3.4.1 RBATCH Configuration -- 3.4.2 RBATCH Specifications -- 3.5 Representation of Nonideal Reactors -- 3.6 RCSTR Convergence -- 3.6.1 Initialization -- 3.6.2 Scaling Factors -- 3.6.3 Residence Time Loop -- 3.6.4 Energy Balance Loop -- 3.6.5 Mass Balance Loop -- 3.6.6 Flash Loop -- 3.6.7 Recommendation for RCSTR Mass Balance Algorithm for Polyolefin Process Simulation -- 3.7 RPLUG/RBATCH Model Convergence -- 3.8 Data Fit (Simulation Data Regression) -- 3.9 Workshop 3.1: Data Fit of Kinetic Parameters for Styrene Polymerization Using Concentration Profile Data -- 3.9.1 Objective -- 3.9.2 A Simplified Kinetic Model for Styrene Polymerization -- 3.9.3 Datasets -- 3.9.4 Simulation Data Regression (Data Fit) -- 3.10 Workshop 3.2: Data Fit of Kinetic Parameters for Styrene Polymerization Using Point Data -- 3.10.1 Objective -- 3.10.2 Dataset -- 3.10.3 Simulation Data Regression (Data Fit) -- References -- Chapter 4 Free Radical Polymerizations: LDPE and EVA. |
4.1 Polymers by Free Radical Polymerization -- 4.2 Kinetics of Free Radical Polymerization -- 4.2.1 Initiator and Its Decomposition‐Rate Parameters -- 4.2.2 Chain Initiation Reactions -- 4.2.3 Chain Propagation Reactions -- 4.2.4 Chain Transfer Reactions -- 4.2.5 Termination Reactions -- 4.2.6 Autoacceleration, Trommsdorff Effect, or Gel Effect -- 4.2.7 Other Free Radical Polymerization Reactions -- 4.3 Thermodynamic Methods and Property Parameter Requirements -- 4.4 Workshop 4.1: Simulation of an Autoclave High‐pressure LDPE Process -- 4.4.1 Objectives -- 4.4.2 Process Flowsheet and Simulation Representation -- 4.4.3 Unit System, Components, and Characterization of Polymer -- 4.4.4 Thermodynamic Methods and Property Parameters for Components, Segment, and Polymer -- 4.4.5 PCES (Physical Constant Estimation System) for Estimating Missing‐Property Parameters -- 4.4.6 Defining Free Radical Polymerization Reactions for LDPE -- 4.4.7 Specifications of Inlet Process Streams and Unit Operation and Reactor Blocks -- 4.4.8 Methodology for Improving Simulation Convergence and for Kinetic Parameter Estimation -- 4.4.9 Base‐Case Simulation Results -- 4.4.10 Model Applications -- 4.4.11 Separation Section -- 4.5 Workshop 4.2: Simulation of Tubular Reactors for HP LDPE Process -- 4.5.1 Objectives -- 4.5.2 Process Flowsheet and Simulation Representation -- 4.5.3 Unit System, Components, and Characterization of Polymer -- 4.5.4 Thermodynamic Method and Property Parameters for Components -- 4.5.5 PCES (Physical Constant Estimation System) for Estimating Missing‐Property Parameters -- 4.5.6 Free Radical Polymerization Reactions for LDPE -- 4.5.7 Specifications |
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of Inlet Process Streams and Unit Operation and Reactor Blocks -- 4.5.8 User FORTRAN Subroutine for Heat Transfer Calculations for the LDPE Reactor. |
4.5.9 Base‐Case Simulation Targets and Kinetic Parameter Estimation. |
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5. |
Record Nr. |
UNINA9910481556203321 |
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Autore |
Copernicus Nicolaus <1473-1543.> |
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Titolo |
Nicolai Copernici Torinensis De reuolutionibus orbium coelestium, libri 6. In quibus stellarum et fixarum et erraticarum motus, ex veteribus atque recentibus obseruationibus, restituit hic autor. Praeterea tabulas expeditas luculentasque addidit, ex quibus eosdem motus ad quoduis tempus mathematum studiosus facillime calculare poterit. Item, de libris reuolutionum Nicolai Copernici narratio prima, per M. Georgium Ioachimum Rheticum ad D. Ioan. Schonerum scripta [[electronic resource]] |
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Pubbl/distr/stampa |
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Basel, : Sebastian Henricpetri, 1546-1627, 1566 |
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Descrizione fisica |
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Online resource ([6], 213, [1] c., 2º) |
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Altri autori (Persone) |
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RhäticusGeorg Joachim <1514-1576.> |
PetriHeinrich <1508-1579.> |
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Lingua di pubblicazione |
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Formato |
Materiale a stampa |
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Livello bibliografico |
Monografia |
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Note generali |
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Reproduction of original in Biblioteca Nazionale Centrale di Firenze. |
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