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Refinery engineering : integrated process modeling and optimization /
This book is a pioneering and comprehensive introduction to the complex subject of integrated refinery process simulation, using many of the tools and techniques currently employed in modern refineries. Adopting a systematic and practical approach, the authors include the theory, case studies and ha...
| Clasificación: | Libro Electrónico |
|---|---|
| Autor principal: | |
| Otros Autores: | , |
| Formato: | Electrónico eBook |
| Idioma: | Inglés |
| Publicado: |
Weinheim :
Wiley-VCH,
©2012.
|
| Temas: | |
| Acceso en línea: | Texto completo |
MARC
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| 100 | 1 | |a Chang, Ai-Fu. | |
| 245 | 1 | 0 | |a Refinery engineering : |b integrated process modeling and optimization / |c Ai-Fu Chang, Kiran Pashikanti, and Y.A. Liu. |
| 260 | |a Weinheim : |b Wiley-VCH, |c ©2012. | ||
| 300 | |a 1 online resource (xxiv, 497 pages) : |b illustrations | ||
| 336 | |a text |b txt |2 rdacontent | ||
| 337 | |a computer |b c |2 rdamedia | ||
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| 504 | |a Includes bibliographical references and index. | ||
| 588 | 0 | |a Print version record. | |
| 520 | |a This book is a pioneering and comprehensive introduction to the complex subject of integrated refinery process simulation, using many of the tools and techniques currently employed in modern refineries. Adopting a systematic and practical approach, the authors include the theory, case studies and hands-on workshops, explaining how to work with real data. As a result, senior-level undergraduate and graduate students, as well as industrial engineers learn how to develop and use the latest computer models for the predictive modeling and optimization of integrated refinery processes. -- |c Edited summary from book. | ||
| 505 | 0 | |a Title Page; Contents; Foreword by Steven R. Cope; Foreword by Lawrence B. Evans; Preface; Acknowledgements; About the Authors; 1 Characterization, Physical and Thermodynamic Properties of Oil Fractions; 1.1 Crude Assay; 1.1.1 Bulk Properties; 1.1.2 Fractional Properties; 1.1.3 Interconversion of Distillation Curves; 1.2 Pseudocomponent Generation Based on Boiling-Point Ranges; 1.3 Workshop 1.1 -- Interconvert Distillation Curves; 1.4 Workshop 1.2 -- Extrapolate an Incomplete Distillation Curve; 1.5 Workshop 1.3 -- Calculate MeABP of a Given Assay. | |
| 505 | 8 | |a 1.6 Workshop 1.4 -- Duplicate the Oil Fraction in Aspen HYSYS Petroleum Refining1.7 Property Requirements for Refinery Process Models; 1.8 Physical Properties; 1.8.1 Estimating Minimal Physical Properties for Pseudocomponents; 1.8.2 Molecular Weight; 1.8.3 Critical Properties; 1.8.4 Liquid Density; 1.8.5 Ideal Gas Heat Capacity; 1.8.6 Other Derived Physical Properties; 1.9 Process Thermodynamics; 1.9.1 Thermodynamic Models; 1.9.2 Mixed or Activity-Coeff icient Approach; 1.9.3 Equation-of-State Approach; 1.10 Miscellaneous Physical Properties for Refinery Modeling. | |
| 505 | 8 | |a 1.10.1 Two Approaches for Estimating Fuel Properties1.10.2 Flash Point; 1.10.3 Freeze Point; 1.10.4 PNA Composition; 1.11 Conclusions; 1.12 Nomenclature; 1.13 References; 2 Atmospheric Distillation Unit; 2.1 Introduction; 2.2 Scope of the Chapter; 2.3 Process Overview; 2.3.1 Desalting; 2.3.2 Preheat Train and Heat Recovery; 2.3.3 Atmospheric Distillation; 2.4 Model Development; 2.5 Feed Characterization; 2.6 Data Requirements and Validation; 2.7 Representative Atmospheric Distillation Unit; 2.8 Building the Model in Aspen HYSYS; 2.8.1 Entering the Crude Information. | |
| 505 | 8 | |a 2.8.2 Selection of a Thermodynamic System2.8.3 Crude Charge and Prefractionation Units; 2.8.4 Atmospheric Distillation Column -- Initial; 2.8.5 Atmospheric Distillation Column -- Side Strippers; 2.8.6 Atmospheric Distillation Column -- Pumparounds; 2.8.7 Atmospheric Distillation Column -- Final Column Convergence; 2.8.8 Post-Convergence; 2.9 Results; 2.10 Model Applications to Process Optimization; 2.10.1 Improve the 5% Distillation Point for an Individual Cut; 2.10.2 Change Yield of a Given Cut; 2.11 Workshop 2.1 -Rebuild Model Using "Back-blending" Procedure. | |
| 505 | 8 | |a 2.11.1 Import Distillation Data into Aspen HYSYS Oil Manager2.11.2 Import Distillation Data into Aspen HYSYS Oil Manager; 2.11.3 Reorganize Process Flowsheet; 2.11.4 Converging Column Model; 2.11.5 Comparison of Results; 2.12 Workshop 2.2 -- Investigate Changes in Product Profiles with New Product Demands; 2.12.1 Update Column Specifications; 2.12.2 Vary Draw Rate of LGO; 2.13 Conclusions; 2.14 Nomenclature; 2.15 References; 3 Vacuum Distillation Unit; 3.1 Process Description; 3.2 Data Reconciliation; 3.2.1 Required Data; 3.2.2 Representation of the Atmospheric Residue. | |
| 546 | |a English. | ||
| 590 | |a ProQuest Ebook Central |b Ebook Central Academic Complete | ||
| 650 | 0 | |a Petroleum |x Refining. | |
| 650 | 6 | |a Pétrole |x Raffinage. | |
| 650 | 7 | |a TECHNOLOGY & ENGINEERING |x Petroleum. |2 bisacsh | |
| 650 | 7 | |a Petroleum |x Refining |2 fast | |
| 700 | 1 | |a Pashikanti, Kiran. | |
| 700 | 1 | |a Liu, Y. A. |q (Yih An) | |
| 758 | |i has work: |a Refinery engineering (Text) |1 https://id.oclc.org/worldcat/entity/E39PCGWxHytGh67KMHy3BrXVQ3 |4 https://id.oclc.org/worldcat/ontology/hasWork | ||
| 776 | 0 | 8 | |i Print version: |z 9781299313590 |
| 856 | 4 | 0 | |u https://ebookcentral.uam.elogim.com/lib/uam-ebooks/detail.action?docID=1143530 |z Texto completo |
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