Refinery engineering : integrated process modeling and optimization /

• 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.

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...

Πίνακας περιεχομένων:

• 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.
• 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.
• 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.
• 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.
• 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.