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1. |
Record Nr. |
UNINA9910544856503321 |
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Autore |
Hunniecutt Jeni Ruth |
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Titolo |
Rethinking Reintegration and Veteran Identity : A New Consciousness / / by Jeni Ruth Hunniecutt |
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Pubbl/distr/stampa |
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Cham : , : Springer International Publishing : , : Imprint : Palgrave Macmillan, , 2022 |
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ISBN |
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9783030937546 |
9783030937539 |
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Edizione |
[1st ed. 2022.] |
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Descrizione fisica |
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1 online resource (223 pages) |
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Disciplina |
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362.19685210086970973 |
362.1086970973 |
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Soggetti |
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Ethnology |
Ethnopsychology |
Ethnography |
Sociocultural Anthropology |
Psychological Anthropology |
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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 contenuto |
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Chapter 1: [The] U.S. Military Veterans: [My] Examination of Identity -- Chapter 2: My Veteran Identity [Crisis]: Suicides And Reintegration -- Chapter 3: Writing Through Layers Of Veteran Liminality -- Chapter 4: Loss Of Community: Searching For And Finding Home -- Chapter 5: Loss Of Structure: Resisting And Finding [My] Voice -- Chapter 6: You Can't Go Back -- Chapter 7: Adapt And Overcome. . |
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Sommario/riassunto |
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This book analyzes and discusses the U.S. Military Veteran identity. Throughout seven chapters spanning narrative, literature, theory and analysis, the book combines the author's own personal story of joining, serving in, and separating from the U.S. military with corresponding research about military transitions, reintegration, Veteran suicides, and psychosocial adjustment challenges. The purpose of the book is to help readers understand Veteran identity in a way that centers the social implications of belonging to and serving in the military institution. In the final chapters of the book, existing theories and models related to military transitions are dissected before a new Model of Veteran |
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Identity Hierarchy as well as a reconceptualization of Veteran identity are presented. |
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2. |
Record Nr. |
UNINA9911019396103321 |
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Autore |
Luyben William L |
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Titolo |
Reactive distillation design and control / / William L. Luyben, Cheng-Ching Yu |
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Pubbl/distr/stampa |
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Hoboken, NJ, : John Wiley, c2008 |
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ISBN |
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9786612112652 |
9781282112650 |
1282112651 |
9780470377741 |
0470377747 |
9780470377796 |
0470377798 |
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Descrizione fisica |
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1 online resource (598 p.) |
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Altri autori (Persone) |
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Disciplina |
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Soggetti |
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Distillation apparatus - Design and construction |
Chemical process control |
Distillation |
Reactivity (Chemistry) |
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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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Nota di contenuto |
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REACTIVE DISTILLATION DESIGN AND CONTROL; CONTENTS; PREFACE; 1 INTRODUCTION; 1.1 History; 1.2 Basics of Reactive Distillation; 1.3 Neat Operation Versus Excess Reactant; 1.4 Limitations; 1.4.1 Temperature Mismatch; 1.4.2 Unfavorable Volatilities; 1.4.3 Slow Reaction Rates; 1.4.4 Other Restrictions; 1.5 Scope; 1.6 Computational Methods; 1.6.1 Matlab Programs for Steady-State Design; 1.6.2 Aspen Simulations; 1.7 Reference Materials; PART I STEADY-STATE DESIGN OF |
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IDEAL QUATERNARY SYSTEM; 2 PARAMETER EFFECTS; 2.1 Effect of Holdup on Reactive Trays; 2.2 Effect of Number of Reactive Trays |
2.3 Effect of Pressure2.4 Effect of Chemical Equilibrium Constant; 2.5 Effect of Relative Volatilities; 2.5.1 Constant Relative Volatilities; 2.5.2 Temperature-Dependent Relative Volatilities; 2.6 Effect of Number of Stripping and Rectifying Trays; 2.7 Effect of Reactant Feed Location; 2.7.1 Reactant A Feed Location (N(FA)); 2.7.2 Reactant B Feed Location (N(FB)); 2.8 Conclusion; 3 ECONOMIC COMPARISON OF REACTIVE DISTILLATION WITH A CONVENTIONAL PROCESS; 3.1 Conventional Multiunit Process; 3.1.1 Assumptions and Specifications; 3.1.2 Steady-State Design Procedure |
3.1.3 Sizing and Economic Equations3.2 Reactive Distillation Design; 3.2.1 Assumptions and Specifications; 3.2.2 Steady-State Design Procedure; 3.3 Results for Different Chemical Equilibrium Constants; 3.3.1 Conventional Process; 3.3.2 Reactive Distillation Process; 3.3.3 Comparisons; 3.4 Results for Temperature-Dependent Relative Volatilities; 3.4.1 Relative Volatilities; 3.4.2 Optimum Steady-State Designs; 3.4.3 Real Chemical Systems; 3.5 Conclusion; 4 NEAT OPERATION VERSUS USING EXCESS REACTANT; 4.1 Introduction; 4.2 Neat Reactive Column; 4.3 Two-Column System with Excess B |
4.3.1 20% Excess B Case4.3.2 10% Excess B Case; 4.4 Two-Column System with 20% Excess of A; 4.5 Economic Comparison; 4.6 Conclusion; PART II STEADY-STATE DESIGN OF OTHER IDEAL SYSTEMS; 5 TERNARY REACTIVE DISTILLATION SYSTEMS; 5.1 Ternary System Without Inerts; 5.1.1 Column Configuration; 5.1.2 Chemistry and Phase Equilibrium Parameters; 5.1.3 Design Parameters and Procedure; 5.1.4 Effect of Pressure; 5.1.5 Holdup on Reactive Trays; 5.1.6 Number of Reactive Trays; 5.1.7 Number of Stripping Trays; 5.2 Ternary System With Inerts; 5.2.1 Column Configuration |
5.2.2 Chemistry and Phase Equilibrium Parameters5.2.3 Design Parameters and Procedure; 5.2.4 Effect of Pressure; 5.2.5 Control Tray Composition; 5.2.6 Reactive Tray Holdup; 5.2.7 Effect of Reflux; 5.2.8 Chemical Equilibrium Constant; 5.2.9 Feed Composition; 5.2.10 Number of Reactive Trays; 5.2.11 Number of Rectifying and Stripping Trays; 5.3 Conclusion; 6 TERNARY DECOMPOSITION REACTION; 6.1 Ternary Decomposition Reaction: Intermediate-Boiling Reactant; 6.1.1 Column Configuration; 6.1.2 Chemistry and Phase Equilibrium Parameters; 6.1.3 Design Parameters and Procedure |
6.1.4 Holdup on Reactive Trays |
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Sommario/riassunto |
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After an overview of the fundamentals, limitations, and scope of reactive distillation, this book uses rigorous models for steady-state design and dynamic analysis of different types of reactive distillation columns and quantitatively compares the economics of reactive distillation columns with conventional multi-unit processes. It goes beyond traditional steady-state design that primarily considers the capital investment and energy costs when analyzing the control structure and the dynamic robustness of disturbances, and discusses how to maximize the economic and environmental benefits of rea |
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