Buch, Englisch, 498 Seiten, Format (B × H): 170 mm x 238 mm, Gewicht: 1014 g
ISBN: 978-3-527-33357-8
Verlag: Wiley VCH Verlag GmbH
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.
Additional material is available online providing relevant spreadsheets and simulation files for all the models and examples presented in the book.
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Weitere Infos & Material
PREFACECHARACTERIZATION, PHYSICAL AND THERMODYNAMIC PROPERTIES OF OIL FRACTIONSCrude AssayPseudocomponent Generation Based on Boiling-Point RangesWorkshop 1.1 - Interconvert Distillation CurvesWorkshop 1.2 - Extrapolate an Incomplete Distillation CurveWorkshop 1.3 - Calculate MeABP of a Given AssayWorkshop 1.4 - Duplicate the Oil Fraction in Aspen HYSYS/RefiningProperty Requirements for Refinery Process ModelsPhysical PropertiesProcess ThermodynamicsMiscellaneous Physical Properties for Refinery ModelingConclusionsNomenclatureReferencesATMOSPHERIC DISTILLATION UNITIntroductionScope of the ChapterProcess OverviewModel DevelopmentFeed CharacterizationData Requirements and ValidationRepresentative Atmospheric Distillation UnitBuilding the Model in Aspen HYSYSResultsModel Applications to Process OptimizationWorkshop 2.1 - Rebuild Model Using "Backblending" ProcedureWorkshop 2.2 - Investigate Changes in Product Profiles with New Product DemandsConclusionsNomenclatureReferencesVACUUM DISTILLATION UNITProcess DescriptionData ReconciliationModel ImplementationModel Applications toProcess Optimization - VDU Deep-Cut OperationWorkshop - Using Aspen HYSYS/Refining to Implement Deep-Cut OperationReferencesPREDICTIVE MODELING OF THE FLUID CATALYTIC CRACKING (FCC) PROCESSIntroductionProcess DescriptionProcess ChemistryLiterature ReviewAspen HYSYS/Petroleum Refining FCC ModelCalibrating the Aspen HYSYS/Petroleum Refining FCC ModelFractionationMapping Feed Information to Kinetic LumpsOverall Modeling StrategyResultsModel Applications to Process OptimizationModel Application to Refinery Production PlanningWorkshop 4.1: Guide for Modeling FCC Units in Aspen HYSYS/Petroleum RefiningWorkshop 4.2: Calibrating Basic FCC ModelWorkshop 4.3: Build Main Fractionator and Gas Plant SystemWorkshop 4.4: Model Applications to Process Optimization -Perform Case Study to Identify Different Gasoline Production ScenariosWorkshop 4.5: Model Application to Production Planning- Generate DELTA-BASE Vectors for Linear-Programming (LP)-Based Production PlanningConclusionsNomenclatureReferencesPREDICTIVE MODELING OF THE CONTINUOUS CATALYST REGENERATION (CCR)REFORMING PROCESSIntroductionProcess OverviewProcess ChemistryLiterature ReviewAspen HYSYS/Petroleum Refining Catalytic Reformer ModelThermophysical PropertiesFractionation SystemFeed CharacterizationModel ImplementationOverall Modeling StrategyResultsModel Applications to Process OptimizationModel Applications to Refinery Production PlanningWorkshop 5.1: Guide for Modeling CCR Units in Aspen HYSYS/Petroleum RefiningWorkshop 5.2: Model CalibrationWorkshop 5.3: Build a Downstream FractionationWorkshop 5.4: Case Study to Vary RON and Product Distribution ProfileConclusionsNomenclatureReferencesPREDICTIVE MODELING OF THE HYDROPROCESSING UNITSIntroductionAspen HYSYS/Refining HCR Modeling ToolProcess DescriptionModel DevelopmentModeling Results of MP HCR ProcessModeling Results of HP HCR ProcessModel Applications to Process OptimizationModel Application - Delta-Base Vector GenerationConclusionWorkshop 6.1 - Build Preliminary Reactor Model of HCR ProcessWorkshop 6.2 - Calibrate Preliminary Reactor Model to Match Plant DataWorkshop 6.3 - Model Applications to Process OptimizationWorkshop 6.4 - Connect Reactor Model to Fractionator SimulationNomenclatureReferences