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درصورت عدم همخوانی توضیحات با کتاب
از ساعت 7 صبح تا 10 شب
ویرایش: [2 ed.]
نویسندگان: Kamal I. M. Al-Malah
سری:
ISBN (شابک) : 1119868696, 9781119868699
ناشر: Wiley
سال نشر: 2022
تعداد صفحات: 656
[658]
زبان: English
فرمت فایل : PDF (درصورت درخواست کاربر به PDF، EPUB یا AZW3 تبدیل می شود)
حجم فایل: 93 Mb
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توجه داشته باشید کتاب Aspen Plus: کاربردهای مهندسی شیمی نسخه زبان اصلی می باشد و کتاب ترجمه شده به فارسی نمی باشد. وبسایت اینترنشنال لایبرری ارائه دهنده کتاب های زبان اصلی می باشد و هیچ گونه کتاب ترجمه شده یا نوشته شده به فارسی را ارائه نمی دهد.
Cover Title Page Copyright Page CONTENTS PREFACE THE BOOK THEME ABOUT THE AUTHOR WHAT DO YOU GET OUT OF THIS BOOK? WHO SHOULD READ THIS BOOK? NOTES FOR INSTRUCTORS ACKNOWLEDGMENT ABOUT THE COMPANION WEBSITE CHAPTER 1 INTRODUCING ASPEN PLUS® WHAT DOES ASPEN STAND FOR? WHAT IS ASPEN PLUS® PROCESS SIMULATION MODEL? LAUNCHING ASPEN PLUS® V12.1 BEGINNING A SIMULATION ENTERING COMPONENTS SPECIFYING THE PROPERTY METHOD IMPROVEMENT OF THE PROPERTY METHOD ACCURACY FILE SAVING A GOOD FLOWSHEETING PRACTICE ASPEN PLUS® BUILT-IN HELP FOR MORE INFORMATION Reference HOMEWORK/CLASSWORK 1.1 (PXY) DIAGRAM HOMEWORK/CLASSWORK 1.2 (ΔGMIX) FOR AN IDEAL AND REAL SYSTEM HOMEWORK/CLASSWORK 1.3 (LIKES DISSOLVE LIKES) AS ENVISAGED BY NRTL PROPERTY METHOD HOMEWORK/CLASSWORK 1.4 THE MIXING RULE FOR THERMODYNAMIC PROPERTIES HOMEWORK/CLASSWORK 1.5 TXXY DIAGRAM FOR TRIETHYLAMINE–WATER SYSTEM HOMEWORK/CLASSWORK 1.6 IBUPROFEN SOLUBILITY IN A HYBRID SOLVENT HOMEWORK/CLASSWORK 1.7 ESTIMATION OF MIXTURE PROPERTIES HOMEWORK/CLASSWORK 1.8 MAPPING THE PROPERTY METHOD WITH THE CHEMICAL PROCESS/COMPONENT HOMEWORK/CLASSWORK 1.9 SPELLING THE PROPERTY METHOD WITH THE CHEMICAL PROCESS/COMPONENT CHAPTER 2 MORE ON ASPEN PLUS® FLOWSHEET FEATURES (1) PROBLEM DESCRIPTION ENTERING AND NAMING COMPOUNDS BINARY INTERACTIONS THE “SIMULATION” ENVIRONMENT: ACTIVATION DASHBOARD PLACING A BLOCK AND MATERIAL STREAM FROM MODEL PALETTE BLOCK AND STREAM MANIPULATION DATA INPUT, PROJECT TITLE, AND REPORT OPTIONS RUNNING THE SIMULATION THE DIFFERENCE AMONG RECOMMENDED PROPERTY METHODS NIST/TDE EXPERIMENTAL DATA ADDING MORE STREAM PROPERTIES HOMEWORK/CLASSWORK 2.1 (WATER–ALCOHOL SYSTEM) HOMEWORK/CLASSWORK 2.2 (WATER–ACETONE–EIPK SYSTEM WITH NIST/DTE DATA) HOMEWORK/CLASSWORK 2.3 (WATER–ACETONE–EIPK SYSTEM WITHOUT NIST/DTE DATA) HOMEWORK/CLASSWORK 2.4 (WATER–SUCROSE SYSTEM) HOMEWORK/CLASSWORK 2.5 (WATER–GLUCOSE SYSTEM) HOMEWORK/CLASSWORK 2.7 (PARAMETERIZED HYDROCARBON SYSTEM) CHAPTER 3 MORE ON ASPEN PLUS® FLOWSHEET FEATURES (2) PROBLEM DESCRIPTION: CONTINUATION TO CHAPTER TWO THE CLEAN PARAMETERS STEP SIMULATION RESULTS CONVERGENCE ADDING STREAM TABLE PROPERTY SETS ADDING STREAM CONDITIONS PRINTING FROM ASPEN PLUS® VIEWING THE INPUT SUMMARY REPORT GENERATION STREAM PROPERTIES ADDING A FLASH SEPARATION UNIT THE REQUIRED INPUT FOR “FLASH3”-TYPE SEPARATOR RUNNING THE SIMULATION AND CHECKING THE RESULTS HOMEWORK/CLASSWORK 3.1 (OUTPUT OF INPUT DATA AND RESULTS) HOMEWORK/CLASSWORK 3.2 (OUTPUT OF INPUT DATA AND RESULTS) HOMEWORK/CLASSWORK 3.3 (OUTPUT OF INPUT DATA AND RESULTS) HOMEWORK/CLASSWORK 3.4 (THE PARTITION COEFFICIENT OF A SOLUTE) HOMEWORK/CLASSWORK 3.5 (A PARAMETERIZED FLASH DRUM) HOMEWORK/CLASSWORK 3.6 (SEPARATION OF HYDROCARBONS USING FLASH DRUMS) HOMEWORK/CLASSWORK 3.7 (A PARAMETERIZED FLASH DRUM) HOMEWORK/CLASSWORK 3.8 (A PARAMETERIZED HYDROCARBONS FLASH DRUM) CHAPTER 4 FLASH SEPARATION AND DISTILLATION COLUMNS PROBLEM DESCRIPTION ADDING A SECOND MIXER AND FLASH DESIGN SPECIFICATIONS STUDY ASPEN PLUS® DISTILLATION COLUMN OPTIONS “DSTWU” DISTILLATION COLUMN “DISTL” DISTILLATION COLUMN “RADFRAC” DISTILLATION COLUMN DESIGN AND SPECIFY COLUMN INTERNALS HOMEWORK/CLASSWORK 4.1 (WATER–ALCOHOL SYSTEM) HOMEWORK/CLASSWORK 4.2 (WATER–ACETONE–EIPK SYSTEM WITH NIST/DTE DATA) HOMEWORK/CLASSWORK 4.3 (WATER–ACETONE–EIPK SYSTEM WITHOUT NIST/DTE DATA) HOMEWORK/CLASSWORK 4.4 (SCRUBBER) HOMEWORK/CLASSWORK 4.5 (CYCLOHEXANE–TOLUENE DISTILLATION) HOMEWORK/CLASSWORK 4.6 (WATER–ETHANOL DISTILLATION) CHAPTER 5 LIQUID–LIQUID EXTRACTION PROCESS PROBLEM DESCRIPTION THE PROPER SELECTION FOR PROPERTY METHOD FOR EXTRACTION PROCESSES DEFINING NEW PROPERTY SETS THE PROPERTY METHOD VALIDATION VERSUS EXPERIMENTAL DATA USING SENSITIVITY ANALYSIS A MULTISTAGE EXTRACTION COLUMN THE TRIANGLE DIAGRAM REFERENCES HOMEWORK/CLASSWORK 5.1 (SEPARATION OF MEK FROM OCTANOL) HOMEWORK/CLASSWORK 5.2 (SEPARATION OF MEK FROM WATER USING OCTANE) HOMEWORK/CLASSWORK 5.3 (SEPARATION OF ACETIC ACID FROM WATER USING ISOPROPYL BUTYL ETHER) HOMEWORK/CLASSWORK 5.4 (SEPARATION OF ACETONE FROM WATER USING TRICHLOROETHANE) HOMEWORK/CLASSWORK 5.5 (SEPARATION OF PROPIONIC ACID FROM WATER USING MEK) HOMEWORK/CLASSWORK 5.6 (SEPARATION OF ETHYL ACETATE FROM WATER USING AN ORGANIC SOLVENT) HOMEWORK/CLASSWORK 5.7 (SEPARATION OF DILUTE ACETIC ACID FROM WATER USING AN ORGANIC SOLVENT) CHAPTER 6 REACTORS WITH SIMPLE REACTION KINETIC FORMS PROBLEM DESCRIPTION DEFINING REACTION RATE CONSTANT TO ASPEN PLUS® ENVIRONMENT ENTERING COMPONENTS AND METHOD OF PROPERTY THE RIGOROUS PLUG FLOW REACTOR (RPLUG) REACTOR AND REACTION SPECIFICATIONS FOR RPLUG (PFR) RUNNING THE SIMULATION (PFR ONLY) EXERCISE 6.1 COMPRESSOR (CMPRSSR) AND RADFRAC RECTIFYING COLUMN (RECTIF) RUNNING THE SIMULATION (PFR + CMPRSSR + RECTIF) EXERCISE 6.2 RADFRAC DISTILLATION COLUMN (DSTL) RUNNING THE SIMULATION (PFR + CMPRSSR + RECTIF + DSTL) REACTOR AND REACTION SPECIFICATIONS FOR RCSTR RUNNING THE SIMULATION (PFR + CMPRSSR + RECTIF + DSTL + RCSTR) EXERCISE 6.3 SENSITIVITY ANALYSIS: THE REACTOR’S OPTIMUM OPERATING CONDITIONS REFERENCES HOMEWORK/CLASSWORK 6.1 (HYDROGEN PEROXIDE SHELF LIFE) HOMEWORK/CLASSWORK 6.2 (ESTERIFICATION PROCESS) HOMEWORK/CLASSWORK 6.3 (LIQUID-PHASEISOMERIZATION OF N-BUTANE) HOMEWORK/CLASSWORK 6.4 (LIQUID-PHASEBIODIESEL FORMATION) HOMEWORK/CLASSWORK 6.5 (TRIMETHYLENE GLYCOL FORMATION) HOMEWORK/CLASSWORK 6.6 (TRIETHYLAMINE FORMATION) HOMEWORK/CLASSWORK 6.7 (N-PROPYLPROPIONATE FORMATION) CHAPTER 7 REACTORS WITH COMPLEX (NONCONVENTIONAL) REACTION KINETIC FORMS PROBLEM DESCRIPTION NONCONVENTIONAL KINETICS: LHHW TYPE REACTION GENERAL EXPRESSIONS FOR SPECIFYING LHHW-TYPE REACTION IN ASPEN PLUS® THE “DRIVING FORCE” FOR THE NONREVERSIBLE (IRREVERSIBLE) CASE THE “DRIVING FORCE” FOR THE REVERSIBLE CASE THE “ADSORPTION EXPRESSION” THE PROPERTY METHOD: “SRK” RPLUG FLOWSHEET FOR METHANOL PRODUCTION ENTERING INPUT PARAMETERS DEFINING METHANOL PRODUCTION REACTIONS AS LHHW TYPE SENSITIVITY ANALYSIS: EFFECT OF TEMPERATURE AND PRESSURE ON SELECTIVITY REFERENCES HOMEWORK/CLASSWORK 7.1 (GAS-PHASEOXIDATION OF CHLOROFORM) HOMEWORK/CLASSWORK 7.2 (FORMATION OF STYRENE FROM ETHYLBENZENE) HOMEWORK/CLASSWORK 7.3 (COMBUSTION OF METHANE OVER STEAM-AGEDPT–PD CATALYST) HOMEWORK/CLASSWORK 7.4 (LHHW KINETICS OF NO OXIDATION OVER CO3O4 CATALYST) HOMEWORK/CLASSWORK 7.5 (LHHW KINETICS OF LIMONENE PEROXIDATION OVER PW-AMBERLITECATALYST) CHAPTER 8 PRESSURE DROP, FRICTION FACTOR, NPSHA, AND CAVITATION PROBLEM DESCRIPTION THE PROPERTY METHOD: “STEAMNBS” A WATER PUMPING FLOWSHEET ENTERING PIPE, PUMP, AND FITTINGS SPECIFICATIONS RESULTS: FRICTIONAL PRESSURE DROP, THE PUMP WORK, VALVE CHOKING, AND ANPSH VERSUS RNPSH EXERCISE 8.1 MODEL ANALYSIS TOOLS: SENSITIVITY FOR THE ONSET OF CAVITATION OR VALVE CHOKING CONDITION REFERENCES HOMEWORK/CLASSWORK 8.1 (PENTANE TRANSPORT) HOMEWORK/CLASSWORK 8.2 (GLYCEROL TRANSPORT) HOMEWORK/CLASSWORK 8.3 (AIR COMPRESSION) HOMEWORK/CLASSWORK 8.4 (LPG COMPRESSION AND STORAGE) HOME/CLASS WORK 8.5 (N2 COMPRESSOR OUTLET PRESSURE) HOMEWORK/CLASSWORK 8.6 (WATER–PROPANOL PUMP) CHAPTER 9 THE OPTIMIZATION TOOL PROBLEM DESCRIPTION: DEFINING THE OBJECTIVE FUNCTION THE PROPERTY METHOD: “STEAMNBS” A FLOWSHEET FOR WATER TRANSPORT ENTERING STREAM, PUMP, AND PIPE SPECIFICATIONS MODEL ANALYSIS TOOLS: THE OPTIMIZATION TOOL MODEL ANALYSIS TOOLS: THE SENSITIVITY TOOL LAST COMMENTS REFERENCES HOMEWORK/CLASSWORK 9.1 (SWAMEE–JAIN EQUATION) HOMEWORK/CLASSWORK 9.2 (A SIMPLIFIED PIPE DIAMETER OPTIMIZATION) HOMEWORK/CLASSWORK 9.3 (THE OPTIMUM DIAMETER FOR A VISCOUS FLOW) HOMEWORK/CLASSWORK 9.4 (THE SELECTIVITY OF PARALLEL REACTIONS) HOMEWORK/CLASSWORK 9.5 (THE INTERMEDIATE PRESSURE OF A TWO-STAGE COMPRESSOR) HOMEWORK/CLASSWORK 9.6 (THE INTERMEDIATE PRESSURE OF A THREE-STAGE COMPRESSOR) CHAPTER 10 HEAT EXCHANGER (H.E.) DESIGN PROBLEM DESCRIPTION TYPES OF HEAT EXCHANGER MODELS IN ASPEN PLUS® THE SIMPLE HEAT EXCHANGER MODEL (“HEATER”) THE RIGOROUS HEAT EXCHANGER MODEL (“HEATX”) THE RIGOROUS EXCHANGER DESIGN AND RATING PROCEDURE The Edr Exchanger Feasibility Panel The Rigorous Mode within the “Heatx” Block GENERAL FOOTNOTES ON EDR EXCHANGER REFERENCES HOMEWORK/CLASSWORK 10.1 (HEAT EXCHANGER WITH PHASE CHANGE) HOMEWORK/CLASSWORK 10.2 (HIGH HEAT DUTY HEAT EXCHANGER) HOMEWORK/CLASSWORK 10.3 (DESIGN SPEC HEAT EXCHANGER) HOMEWORK/CLASSWORK 10.4 (AIR-FINNED HEAT EXCHANGER FOR COCONUT OIL FATTY ACIDS) HOMEWORK/CLASSWORK 10.5 (WATER-COOLED HEAT EXCHANGER FOR COCONUT OIL FATTY ACIDS) HOMEWORK/CLASSWORK 10.6 (OPTIMUM COMPOSITION FOR GLYCEROL–WATER SYSTEM) HOMEWORK/CLASSWORK 10.7 (A SIMPLE WATER HEATER SYSTEM) CHAPTER 11 ELECTROLYTES PROBLEM DESCRIPTION: WATER DE-SOURING WHAT IS AN ELECTROLYTE? THE PROPERTY METHOD FOR ELECTROLYTES THE ELECTROLYTE WIZARD WATER DE-SOURING PROCESS FLOWSHEET ENTERING THE SPECIFICATIONS OF FEED STREAMS AND THE STRIPPER THE SYMMETRIC REFERENCE STATE FOR IONIC COMPONENTS APPENDIX: DEVELOPMENT OF “ELECNRTL” MODEL REFERENCES HOMEWORK/CLASSWORK 11.1 (AN ACIDIC SLUDGE NEUTRALIZATION) HOMEWORK/CLASSWORK 11.2 (CO2 REMOVAL FROM NATURAL GAS) HOMEWORK/CLASSWORK 11.3 (PH OF AQUEOUS SOLUTIONS OF SALTS) HOMEWORK/CLASSWORK 11.4 (PH CURVE FOR A STRONG ACID-STRONG BASE TITRATION) HOMEWORK/CLASSWORK 11.5 (PH CURVE FOR A WEAK ACID–STRONG BASE TITRATION) HOMEWORK/CLASSWORK 11.6 (PH CURVE FOR A STRONG ACID–WEAK BASE TITRATION) HOMEWORK/CLASSWORK 11.7 (NACL AQUEOUS SOLUBILITY) CHAPTER 12 POLYMERIZATION PROCESSES THE THEORETICAL BACKGROUND Polymerization Reactions CATALYST TYPES Ethylene Process Types Reaction Kinetic Scheme Reaction Steps Catalyst States HIGH-DENSITY POLYETHYLENE (HDPE) HIGH-TEMPERATURE SOLUTION PROCESS Problem Definition Process Conditions CREATING ASPEN PLUS® FLOWSHEET FOR HDPE IMPROVING CONVERGENCE PRESENTING THE PROPERTY DISTRIBUTION OF POLYMER HOMEWORK/CLASSWORK 12.1 MAXIMIZING THE DEGREE OF HDPE POLYMERIZATION HOMEWORK/CLASSWORK 12.2 STYRENE ACRYLO-NITRILE (SAN) POLYMERIZATION HOMEWORK/CLASSWORK 12.3 DEGREE OF HDPE POLYMERIZATION WITH RECYCLING HOMEWORK/CLASSWORK 12.4 SOLUBILIZATION OF HDPE IN BENZENE–TOLUENE–HEXANE SOLVENT HOMEWORK/CLASSWORK 12.5 SOLUBILIZATION OF HDPE AND PP IN BENZENE–TOLUENE–HEXANE SOLVENT HOMEWORK/CLASSWORK 12.6 SOLUBILIZATION OF HDPE + PP+PVC IN BENZENE–TOLUENE–HEXANE–ETHANOL SOLVENT HOMEWORK/CLASSWORK 12.7 MAXIMIZATION OF MWN OF PP SYNTHESIS REFERENCES APPENDIX A THE MAIN FEATURES AND ASSUMPTIONS OF ASPEN PLUS® CHAIN POLYMERIZATION MODEL Polymerization Mechanism Copolymerization Mechanism Rate Expressions Rate Constants Catalyst Pre-Activation Catalyst Site Activation Site Activation Reactions Chain Initiation Propagation Chain Transfer to Small Molecules Chain Transfer to Monomer Site Deactivation Site Inhibition Cocatalyst Poisoning Terminal Double-Bond Polymerization Phase Equilibria Rate Calculations Calculated Polymer Properties APPENDIX B THE NUMBER AVERAGE MOLECULAR WEIGHT (MWN) AND WEIGHT AVERAGE MOLECULAR WEIGHT (MWW) CHAPTER 13 CHARACTERIZATION OF DRUG-LIKE MOLECULES AND THEIR SOLUBILITY INTRODUCTION PROBLEM DESCRIPTION CREATING ASPEN PLUS® (AP) PHARMACEUTICAL TEMPLATE Entering the User-Defined Benzamide (BNZMD-UD) as Conventional Specifying Properties to Estimate DEFINING MOLECULAR STRUCTURE OF BNZMD-UD ENTERING PROPERTY DATA CONTRASTING AP DATABANK (BNZMD-DB) VERSUS BNZMD-UD SOLUBILITY OF DRUGS IN A HYBRID SOLVENT FINAL NOTES ON DRUG SOLUBILITY REFERENCES HOMEWORK/CLASSWORK 13.1 (VANILLIN) HOMEWORK/CLASSWORK 13.2 (IBUPROFEN) HOMEWORK/CLASSWORK 13.3 OPTIMUM FORMULATION FOR IBUPROFEN SOLUBILITY IN A HYBRID SOLVENT HOMEWORK/CLASSWORK 13.4 OPTIMUM FORMULATION FOR KETOPROFEN SOLUBILITY IN A HYBRID SOLVENT HOMEWORK/CLASSWORK 13.5 OPTIMUM FORMULATION FOR NAPROXEN SOLUBILITY IN A HYBRID SOLVENT CHAPTER 14 SOLIDS HANDLING INTRODUCTION CREATING ASPEN PLUS® FLOWSHEET Entering Components Information Adding the Flowsheet Objects Defining the Particle Size Distribution (PSD) Calculation of the Outlet PSD EXERCISE 14.1 (DETERMINE CRUSHER OUTLET PSD FROM COMMINUTION POWER) EXERCISE 14.2 (SPECIFYING CRUSHER OUTLET PSD) CREATING ASPEN PLUS® FLOWSHEET Entering Components Information Adding the Flowsheet Objects Entering Input Data Results EXERCISE 14.3 (RE-CONVERGINGTHE SOLUTION FOR AN INPUT CHANGE) REFERENCES HOMEWORK/CLASSWORK 14.1 (KCL DRYING) HOMEWORK/CLASSWORK 14.2 (KCL CRYSTALLIZATION) HOMEWORK/CLASSWORK 14.3 (TPA CRYSTALLIZATION AND AIR DRYING) HOMEWORK/CLASSWORK 14.4 (AGGLOMERATION OF CASO4 AND CACO3 USING LYSINE) HOMEWORK/CLASSWORK 14.5 (ALUMINA TRANSFORMATION WITH RECYCLING) SOLIDS UNIT OPERATIONS Unit Operation Solids Models Solids Separators Models Solids Handling Models SOLIDS CLASSIFICATION PREDEFINED STREAM CLASSIFICATION SUB-STREAM CLASSES PARTICLE SIZE DISTRIBUTION (PSD) FLUIDIZED BEDS CHAPTER 15 ASPEN PLUS® DYNAMICS INTRODUCTION PROBLEM DESCRIPTION PREPARING ASPEN PLUS® SIMULATION FOR ASPEN PLUS® DYNAMICS (APD) CONVERSION OF ASPEN PLUS® STEADY STATE INTO DYNAMIC SIMULATION MODES OF DYNAMIC CSTR HEAT TRANSFER CREATING THE PRESSURE-DRIVEN DYNAMIC FILES FOR APD OPENING A DYNAMIC FILE USING APD THE “SIMULATION MESSAGES” WINDOW THE RUNNING MODE: INITIALIZATION ADDING TEMPERATURE CONTROL (TC) SNAPSHOTS MANAGEMENT FOR CAPTURED SUCCESSFUL OLD RUNS THE CONTROLLER FACEPLATE COMMUNICATION TIME FOR UPDATING/PRESENTING RESULTS THE CLOSED-LOOP AUTO-TUNE VARIATION (ATV) TEST VERSUS OPEN-LOOP TUNE-UP TEST THE OPEN-LOOP (MANUAL MODE) TUNE-UP FOR LIQUID-LEVEL CONTROLLER THE CLOSED-LOOP DYNAMIC RESPONSE FOR LIQUID-LEVEL LOAD DISTURBANCE THE CLOSED-LOOP DYNAMIC RESPONSE FOR LIQUID-LEVEL SET-POINT DISTURBANCE ACCOUNTING FOR DEAD/LAG TIME IN PROCESS DYNAMICS THE CLOSED-LOOP (AUTO MODE) ATV TEST FOR TEMPERATURE CONTROLLER (TC) THE CLOSED-LOOP DYNAMIC RESPONSE: “TC” RESPONSE TO TEMPERATURE LOAD DISTURBANCE INTERACTIONS BETWEEN “LC” AND “TC” CONTROL UNIT THE STABILITY OF A PROCESS WITHOUT CONTROL THE CASCADE CONTROL MONITORING OF VARIABLES AS FUNCTIONS OF TIME FINAL NOTES ON THE VIRTUAL (DRY) PROCESS CONTROL IN APD REFERENCES HOMEWORK/CLASSWORK 15.1 (A CASCADE CONTROL OF A SIMPLE WATER HEATER) HOMEWORK/CLASSWORK 15.2 (A CSTR CONTROL WITH “LMTD” HEAT TRANSFER OPTION) HOMEWORK/CLASSWORK 15.3 (A PFR CONTROL FOR ETHYL-BENZENE PRODUCTION) HOMEWORK/CLASSWORK 15.4 (A PFR CONTROL FOR ETHYLBENZENE PRODUCTION WITH COOLING WATER) HOMEWORK/CLASSWORK 15.5 (WATER HEATING TANK WITH NEGLIGIBLE THERMAL INERTIA) HOMEWORK/CLASSWORK 15.6 (WATER HEATING TANK WITH WEIGHTY THERMAL INERTIA) CHAPTER 16 SAFETY AND ENERGY ASPECTS OF CHEMICAL PROCESSES INTRODUCTION PROBLEM DESCRIPTION ADDING A PRESSURE SAFETY VALVE (PSV) ADDING A RUPTURE DISK (RD) PRESSURE RELIEF PREPARATION OF FLOWSHEET FOR “ENERGY ANALYSIS” ENVIRONMENT THE “ENERGY ANALYSIS” ACTIVATION ASPEN ENERGY ANALYZER HOMEWORK/CLASSWORK 16.1 (ACETONE–WATER SYSTEM: ADDING A STORAGE TANK PROTECTION) HOMEWORK/CLASSWORK 16.2 (ACETONE–WATER SYSTEM: ENERGY ANALYSIS) HOMEWORK/CLASSWORK 16.3 (SEPARATION OF C2/C3/C4 HYDROCARBON MIXTURE: SAFETY AND ENERGY ANALYSIS) HOMEWORK/CLASSWORK 16.4 (SEPARATION OF BENZENE, TOLUENE, AND ETHYLBENZENE MIXTURE: SAFETY AND ENERGY ANALYSIS) HOMEWORK/CLASSWORK 16.5 (CO2, C2, AND C3 GAS HEATER: PRESSURE RELIEF DEVICES) HOMEWORK/CLASSWORK 16.6 (CO2, C2, AND C3 GAS HEATER: ENERGY ANALYSIS) CHAPTER 17 ASPEN PROCESS ECONOMIC ANALYZER (APEA) OPTIMIZED PROCESS FLOWSHEET FOR ACETIC ANHYDRIDE PRODUCTION COSTING OPTIONS IN ASPEN PLUS® ASPEN PROCESS ECONOMIC ANALYZER (APEA) ESTIMATION TEMPLATE FEED AND PRODUCT STREAM PRICES Utility Association with a Flowsheet Block THE FIRST ROUTE FOR CHEMICAL PROCESS COSTING THE SECOND ROUND FOR CHEMICAL PROCESS COSTING Project Properties Loading Simulator Data Mapping and Sizing Project Evaluation Fixing Geometrical Design-Related Errors Executive Summary Capital Costs Report Investment Analysis HOMEWORK/CLASSWORK 17.1 (FEED/PRODUCT UNIT PRICE EFFECT ON PROCESS PROFITABILITY) HOMEWORK/CLASSWORK 17.2 (USING EUROPEAN ECONOMIC TEMPLATE) HOMEWORK/CLASSWORK 17.3 (PROCESS PROFITABILITY OF ACETONE RECOVERY FROM SPENT SOLVENT) HOMEWORK/CLASSWORK 17.4 (PROCESS PROFITABILITY OF ACETONE RECOVERY FROM SPENT SOLVENT WITH RECYCLING) HOMEWORK/CLASSWORK 17.5 (PROCESS PROFITABILITY OF ACETONER ECOVERY FROM SPENT SOLVENT USING KETONE WITH RECYCLING) APPENDIX NET PRESENT VALUE (NPV) FOR A CHEMICAL PLANT DISCOUNTED PAYOUT (PAYBACK) PERIOD (DPP) EXAMPLE 17.1 (UNIFORM CASH FLOW) EXAMPLE 17.2 (NONUNIFORM CASH FLOW) PROFITABILITY INDEX EXAMPLE 17.3 INTERNAL RATE OF RETURN (IRR) MODIFIED INTERNAL RATE OF RETURN (MIRR) EXAMPLE 17.4 CHAPTER 18 TERM PROJECTS (TP) WITH ADVANCED AP FEATURES A GENERAL NOTE ON OIL-WATER SYSTEMS TP #1: PRODUCTION OF ACETONE VIA THE DEHYDRATION OF ISOPROPANOL TP #2: PRODUCTION OF FORMALDEHYDE FROM METHANOL (SENSITIVITY ANALYSIS) TP #3: PRODUCTION OF DIMETHYL ETHER (PROCESS ECONOMICS AND CONTROL) PROCESS DYNAMICS AND CONTROL TP #4: PRODUCTION OF ACETIC ACID VIA PARTIAL OXIDATION OF ETHYLENE GAS TP #5: PYROLYSIS OF BENZENE TP #6: REUSE OF SPENT SOLVENTS TP #7: SOLIDS HANDLING: PRODUCTION OF POTASSIUM SULFATE FROM SODIUM SULFATE TP #8: SOLIDS HANDLING: PRODUCTION OF CACO3-BASED AGGLOMERATE AS A GENERAL ADDITIVE TP #9: SOLIDS HANDLING: FORMULATION OF DIAMMONIUM PHOSPHATE AND POTASSIUM NITRATE BLEND FERTILIZER TP #10: “FLOWSHEETING OPTIONS” | “CALCULATOR”: GAS DE-SOURING AND SWEETENING PROCESS TP #11: USING MORE THAN ONE PROPERTY METHOD AND STREAM CLASS: SOLID-CATALYZED DIRECT HYDRATION OF PROPYLENE TO ISOPROPYL ALCOHOL (IPA) TP #12: POLYMERIZATION: PRODUCTION OF POLYVINYL ACETATE (PVAC) TP #13: POLYMERIZATION: EMULSION COPOLYMERIZATION OF STYRENE AND BUTADIENE TO PRODUCE SBR TP #14: POLYMERIZATION: FREE RADICAL POLYMERIZATION OF METHYL METHACRYLATE TO PRODUCE POLY (METHYL METHACRYLATE) TP #15: LHHW KINETICS: PRODUCTION OF CYCLOHEXANONE-OXIME (CYCHXOXM) VIA CYCLOHEXANONE AMMOXIMATION USING CLAY-BASED TITANIUM SILICALITE (TS) CATALYST TP #16: ACRYLIC ACID PRODUCTION FROM PROPYLENE OXIDATION TP #17: AMMONIA PRODUCTION AT RELATIVELY LOW PRESSURE AND TEMPERATURE TP #18: ACROLEIN PRODUCTION FROM PROPYLENE OXIDATION CHAPTER 19 ASPEN CUSTOM MODELER (ACM) INTRODUCTION SETUP PROPERTIES Start from Aspen Properties Start from Aspen Plus® STARTING ACM ACM TERMINOLOGY Variables Parameters Ports Blocks Connections Streams Procedures MODEL CREATION CREATION OF VARIABLES AND EQUATIONS Specifications for Variables COMPILE AND TEST THE MODEL BUILDING A FLOWSHEET OPEN SYSTEM: ADD THE COMPONENT MOLE BALANCE ADD THE ENERGY BALANCE ADD PORTS MIXING RULE FOR PORTS/STREAMS HANDLING SIMULATION DIVERGENCE PROBLEMS RUNNING ACM MODELS UNDER ASPEN PLUS® (AP) PLATFORM Equivalencing Solvers and Decomposition Using Compatible Port Types Specifying Export Model Properties Create a Default Icon for ACM Model Package Model for Aspen Plus®/HYSYS ACM Model Management Making Use of ACM Model in AP MASS TRANSFER-CONTROLLED EVAPORATION RATE PROCESS DYNAMICS MODEL ADDING A PLOT FORM SCRIPTS AND TASKS Create a Flowsheet Script from Variable Find Create a Flowsheet Task OPTIMIZATION Creating the Dynamic Optimization Inputs Creating a Task to Implement the Optimal Profiles Creating Different Constraints DYNAMIC/STEADY ESTIMATION Creating the Dynamic/Static Estimation Inputs HOMEWORK/CLASSWORK 19.1 FLASH DRUM FOR EG, TEG, AND WATER HOMEWORK/CLASSWORK 19.2 DYNAMIC OPTIMIZATION FOR NON-ISOTHERMAL CSTR REFERENCES INDEX EULA