Refinery engineering : integrated process modeling and optimization /

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...

Πλήρης περιγραφή

Λεπτομέρειες βιβλιογραφικής εγγραφής
Κύριος συγγραφέας: Chang, Ai-Fu
Άλλοι συγγραφείς: Pashikanti, Kiran, Liu, Y. A. (Yih An)
Μορφή: Ηλ. βιβλίο
Γλώσσα:English
Έκδοση: Weinheim : Wiley-VCH, [2012]
Θέματα:
Petroleum > Refining.
TECHNOLOGY & ENGINEERING > Petroleum.
Electronic books.
Διαθέσιμο Online:Full Text via HEAL-Link
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049 |a MAIN 
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. 
264 1 |a Weinheim :  |b Wiley-VCH,  |c [2012] 
264 4 |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 
338 |a online resource  |b cr  |2 rdacarrier 
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. 
650 0 |a Petroleum  |x Refining. 
650 4 |a Petroleum  |x Refining. 
650 7 |a TECHNOLOGY & ENGINEERING  |x Petroleum.  |2 bisacsh 
650 7 |a Petroleum  |x Refining.  |2 fast  |0 (OCoLC)fst01059331 
655 4 |a Electronic books. 
700 1 |a Pashikanti, Kiran. 
700 1 |a Liu, Y. A.  |q (Yih An) 
776 0 8 |i Print version:  |z 9781299313590 
856 4 0 |u https://doi.org/10.1002/9783527666836  |z Full Text via HEAL-Link 
994 |a 92  |b DG1 

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