{"product_id":"aspen-plus-isbn-9781119868699","title":"Aspen Plus","description":"\u003cb\u003eASPEN PLUS\u003csup\u003e®\u003c\/sup\u003e\u003c\/b\u003e \u003cp\u003e\u003cb\u003eComprehensive resource covering Aspen Plus V12.1 and demonstrating how to implement the program in versatile chemical process industries\u003c\/b\u003e \u003c\/p\u003e\u003cp\u003e\u003ci\u003eAspen Plus\u003csup\u003e®\u003c\/sup\u003e: Chemical Engineering Applications\u003c\/i\u003e facilitates the process of learning and later mastering Aspen Plus\u003csup\u003e®\u003c\/sup\u003e, the market-leading chemical process modeling software, with step-by-step examples and succinct explanations. The text enables readers to identify solutions to various process engineering problems via screenshots of the Aspen Plus\u003csup\u003e®\u003c\/sup\u003e platforms in parallel with the related text. \u003c\/p\u003e\u003cp\u003eTo aid in information retention, the text includes end-of-chapter problems and term project problems, online exam and quiz problems for instructors that are parametrized (i.e., adjustable) so that each student will have a standalone version, and extra online material for students, such as Aspen Plus\u003csup\u003e®\u003c\/sup\u003e-related files, that are used in the working tutorials throughout the entire textbook. \u003c\/p\u003e\u003cp\u003eThe second edition of \u003ci\u003eAspen Plus\u003c\/i\u003e\u003csup\u003e®\u003c\/sup\u003e: \u003ci\u003eChemical Engineering Applications\u003c\/i\u003e includes information on: \u003c\/p\u003e\u003cul\u003e\n\u003cli\u003eVarious new features that were embedded into Aspen Plus V12.1 and existing features which have been modified\u003c\/li\u003e \u003cli\u003eAspen Custom Modeler (ACM), covering basic features to show how to merge customized models into Aspen Plus simulator\u003c\/li\u003e \u003cli\u003eNew updates to process dynamics and control and process economic analysis since the first edition was published\u003c\/li\u003e \u003cli\u003eVital areas of interest in relation to the software, such as polymerization, drug solubility, solids handling, safety measures, and energy saving \u003c\/li\u003e\n\u003c\/ul\u003e \u003cp\u003eFor chemical engineering students and industry professionals, the second edition of \u003ci\u003eAspen Plus\u003csup\u003e®\u003c\/sup\u003e: Chemical Engineering Applications\u003c\/i\u003e is a key resource for understanding Aspen Plus and the new features that were added in version 12.1 of the software. Many supplementary learning resources help aid the reader with information retention. \u003c\/p\u003e\u003cp\u003e\u003cb\u003eCh1. Introducing Aspen Plus\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e1.1 What does ASPEN stand for?\u003c\/p\u003e \u003cp\u003e1.2 What is Aspen Plus Process Simulation Model?\u003c\/p\u003e \u003cp\u003e1.3 Launching Aspen Plus V12.0\u003c\/p\u003e \u003cp\u003e1.4 Beginning a Simulation\u003c\/p\u003e \u003cp\u003e1.5 Entering Components\u003c\/p\u003e \u003cp\u003e1.6 Specifying the Property Method\u003c\/p\u003e \u003cp\u003e1.7 Improvement of the Property Method Accuracy\u003c\/p\u003e \u003cp\u003e1.8 File Saving\u003c\/p\u003e \u003cp\u003e1.9 Exercise 1.1\u003c\/p\u003e \u003cp\u003e1.10 Good Flowsheeting Practice\u003c\/p\u003e \u003cp\u003e1.11 Aspen Plus Built-in Help\u003c\/p\u003e \u003cp\u003e1.12 For More Information\u003c\/p\u003e \u003cp\u003e1.13 Home\/Class Work 1.1 (Pxy)\u003c\/p\u003e \u003cp\u003e1.14 Home\/Class Work 1.2 (Gmix)\u003c\/p\u003e \u003cp\u003e1.15 Home\/Class Work 1.3 (Likes Dissolve Likes) as Envisaged by NRTL Property Method\u003c\/p\u003e \u003cp\u003e1.16 Home\/Class Work 1.4 (The Mixing Rule)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh2. More on Aspen Plus Flowsheet Features (1)\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e2.1 Problem Description\u003c\/p\u003e \u003cp\u003e2.2 Entering and Naming Compounds\u003c\/p\u003e \u003cp\u003e2.3 Binary Interactions\u003c\/p\u003e \u003cp\u003e2.4 The “Simulation” Environment: Activation Dashboard\u003c\/p\u003e \u003cp\u003e2.5 Placing a Block and Material Stream from Model Palette\u003c\/p\u003e \u003cp\u003e2.6 Block and Stream Manipulation\u003c\/p\u003e \u003cp\u003e2.7 Data Input, Project Title, \u0026amp; Report Options\u003c\/p\u003e \u003cp\u003e2.8 Running the Simulation\u003c\/p\u003e \u003cp\u003e2.9 The Difference among Recommended Property Methods\u003c\/p\u003e \u003cp\u003e2.10 NIST\/TDE Experimental Data\u003c\/p\u003e \u003cp\u003e2.11 Home-\/Class-Work 2.1 (Water-Alcohol System)\u003c\/p\u003e \u003cp\u003e2.12 Home-\/Class-Work 2.2 (Water-Acetone-EIPK System with NIST\/DTE Data)\u003c\/p\u003e \u003cp\u003e2.13 Home-\/Class-Work 2.3 (Water-Acetone-EIPK System without NIST\/DTE Data)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh3. More on Aspen Plus Flowsheet Features (2)\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e3.1 Problem Description: Continuation to Chapter Two Problem\u003c\/p\u003e \u003cp\u003e3.2 The Clean Parameters Step\u003c\/p\u003e \u003cp\u003e3.3 Simulation Results Convergence\u003c\/p\u003e \u003cp\u003e3.4 Adding Stream Table\u003c\/p\u003e \u003cp\u003e3.5 Property Sets\u003c\/p\u003e \u003cp\u003e3.6 Adding Stream Conditions\u003c\/p\u003e \u003cp\u003e3.7 Printing from Aspen Plus\u003c\/p\u003e \u003cp\u003e3.8 Viewing the Input Summary\u003c\/p\u003e \u003cp\u003e3.9 Report Generation\u003c\/p\u003e \u003cp\u003e3.10 Stream Properties\u003c\/p\u003e \u003cp\u003e3.11 Adding a Flash Separation Unit\u003c\/p\u003e \u003cp\u003e3.12 The Required Input for “Flash3”-Type Separator\u003c\/p\u003e \u003cp\u003e3.13 Running the Simulation and Checking the Results\u003c\/p\u003e \u003cp\u003e3.14 Home-\/Class-Work 3.1 (Output of Input Data \u0026amp; Results)\u003c\/p\u003e \u003cp\u003e3.15 Home-\/Class-Work 3.2 (Output of Input Data \u0026amp; Results)\u003c\/p\u003e \u003cp\u003e3.16 Home-\/Class-Work 3.3 (Output of Input Data \u0026amp; Results)\u003c\/p\u003e \u003cp\u003e3.17 Home-\/Class-Work 3.4 (The Partition Coefficient of a Solute)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh4. Flash Separation \u0026amp; Distillation Columns\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e4.1 Problem Description\u003c\/p\u003e \u003cp\u003e4.2 Adding a Second Mixer and Flash\u003c\/p\u003e \u003cp\u003e4.3 Design Specifications Study\u003c\/p\u003e \u003cp\u003e4.4 Exercise 4.1 (Design Spec)\u003c\/p\u003e \u003cp\u003e4.5 Aspen Plus Distillation Column Options\u003c\/p\u003e \u003cp\u003e4.6 “DSTWU” Distillation Column\u003c\/p\u003e \u003cp\u003e4.7 “Distl” Distillation column\u003c\/p\u003e \u003cp\u003e4.8 “RadFrac” Distillation Column\u003c\/p\u003e \u003cp\u003e4.9 Home\/Class Work 4.1 (Water-Alcohol System)\u003c\/p\u003e \u003cp\u003e4.10 Home\/Class Work 4.2 (Water-Acetone-EIPK System with NIST\/DTE Data)\u003c\/p\u003e \u003cp\u003e4.11 Home\/Class Work 4.2 (Water-Acetone-EIPK System without NIST\/DTE Data)\u003c\/p\u003e \u003cp\u003e4.12 Home\/Class Work 4.4 (Scrubber)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh5. Liquid-Liquid Extraction Process\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e5.1 Problem Description\u003c\/p\u003e \u003cp\u003e5.2 The Proper Selection for Property Method for Extraction Processes\u003c\/p\u003e \u003cp\u003e5.3 Defining New Property Sets\u003c\/p\u003e \u003cp\u003e5.4 Property Method Validation versus Experimental Data Using Sensitivity Analysis\u003c\/p\u003e \u003cp\u003e5.5 A Multi-Stage Extraction Column\u003c\/p\u003e \u003cp\u003e5.6 The Triangle Diagram\u003c\/p\u003e \u003cp\u003e5.7 References\u003c\/p\u003e \u003cp\u003e5.8 Home\/Class Work 5.1 (Separation of MEK from Octanol)\u003c\/p\u003e \u003cp\u003e5.9 Home\/Class Work 5.2 (Separation of MEK from Water Using Octane)\u003c\/p\u003e \u003cp\u003e5.10 Home\/Class Work 5.3 (Separation of Acetic Acid from Water Using Iso-Propyl Butyl Ether)\u003c\/p\u003e \u003cp\u003e5.11 Home\/Class Work 5.4 (Separation of Acetone from Water Using Tri-Chloro-Ethane)\u003c\/p\u003e \u003cp\u003e5.12 Home\/Class Work 5.5 (Separation of Propionic Acid from Water Using MEK)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh6. Reactors with Simple Reaction Kinetic Forms\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e6.1 Problem Description\u003c\/p\u003e \u003cp\u003e6.2 Defining Reaction Rate Constant to Aspen Plus Environment\u003c\/p\u003e \u003cp\u003e6.3 Entering Components and Method of Property\u003c\/p\u003e \u003cp\u003e6.4 The Rigorous Plug Flow Reactor (RPLUG)\u003c\/p\u003e \u003cp\u003e6.5 Reactor and Reaction Specifications for RPLUG (PFR)\u003c\/p\u003e \u003cp\u003e6.6 Running the Simulation (PFR Only)\u003c\/p\u003e \u003cp\u003e6.7 Exercise 6.1\u003c\/p\u003e \u003cp\u003e6.8 Compressor (CMPRSSR) and RadFrac Rectifying Column (RECTIF)\u003c\/p\u003e \u003cp\u003e6.9 Running the Simulation (PFR + CMPRSSR + RECTIF)\u003c\/p\u003e \u003cp\u003e6.10 Exercise 6.2\u003c\/p\u003e \u003cp\u003e6.11 RadFrac Distillation Column (DSTL)\u003c\/p\u003e \u003cp\u003e6.12 Running the Simulation (PFR + CMPRSSR + RECTIF+DSTL)\u003c\/p\u003e \u003cp\u003e6.13 Reactor and Reaction Specifications for RCSTR\u003c\/p\u003e \u003cp\u003e6.14 Running the Simulation (PFR + CMPRSSR + RECTIF+DSTL+RCSTR)\u003c\/p\u003e \u003cp\u003e6.15 Exercise 6.3\u003c\/p\u003e \u003cp\u003e6.16 Sensitivity Analysis: The Reactor’s Optimum Operating Conditions\u003c\/p\u003e \u003cp\u003e6.17 References\u003c\/p\u003e \u003cp\u003e6.18 Home\/Class Work 6.1 (Hydrogen Peroxide Shelf-Life)\u003c\/p\u003e \u003cp\u003e6.19 Home\/Class Work 6.2 (Esterification Process)\u003c\/p\u003e \u003cp\u003e6.20 Home\/Class Work 6.3 (Liquid-Phase Isomerization of n-Butane)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh7. Reactors with Complex (Non-Conventional) Reaction Kinetic Forms\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e7.1 Problem Description\u003c\/p\u003e \u003cp\u003e7.2 Non-Conventional Kinetics: LHHW Type Reaction\u003c\/p\u003e \u003cp\u003e7.3 General Expressions for Specifying LHHW Type Reaction in Aspen Plus\u003c\/p\u003e \u003cp\u003e7.3.1 The “Driving Force” for the Non-Reversible (Irreversible) Case\u003c\/p\u003e \u003cp\u003e7.3.2 The “Driving Force” for the Reversible Case\u003c\/p\u003e \u003cp\u003e7.3.3 The “Adsorption Expression”\u003c\/p\u003e \u003cp\u003e7.4 The Property Method: “SRK”\u003c\/p\u003e \u003cp\u003e7.5 RPLUG Flowsheet for Methanol Production\u003c\/p\u003e \u003cp\u003e7.6 Entering Input Parameters\u003c\/p\u003e \u003cp\u003e7.7 Defining Methanol Production Reactions as LHHW Type\u003c\/p\u003e \u003cp\u003e7.8 Sensitivity Analysis: Effect of Temperature and Pressure on Selectivity\u003c\/p\u003e \u003cp\u003e7.9 References\u003c\/p\u003e \u003cp\u003e7.10 Home\/Class Work 7.1 (Gas-Phase Oxidation of Chloroform)\u003c\/p\u003e \u003cp\u003e7.11 Home\/Class Work 7.2 (Formation of Styrene from Ethyl-Benzene)\u003c\/p\u003e \u003cp\u003e7.12 Home\/Class Work 7.3 (Combustion of Methane over Steam-Aged Pt-Pd Catalyst)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh8. Pressure Drop, Friction Factor, NPSHA, and Cavitation\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e8.1 Problem Description\u003c\/p\u003e \u003cp\u003e8.2 The Property Method: “STEAMNBS”\u003c\/p\u003e \u003cp\u003e8.3 A Water Pumping Flowsheet\u003c\/p\u003e \u003cp\u003e8.4 Entering Pipe, Pump, \u0026amp; Fittings Specifications\u003c\/p\u003e \u003cp\u003e8.5 Results: Frictional Pressure Drop, the Pump Work, Valve Choking, and ANPSH versus RNPSH\u003c\/p\u003e \u003cp\u003e8.6 Exercise 8.1\u003c\/p\u003e \u003cp\u003e8.7 Model Analysis Tools: Sensitivity for the Onset of Cavitation or Valve Choking Condition\u003c\/p\u003e \u003cp\u003e8.8 References\u003c\/p\u003e \u003cp\u003e8.9 Home\/Class Work 8.1 (Pentane Transport)\u003c\/p\u003e \u003cp\u003e8.10 Home\/Class Work 8.2 (Glycerol Transport)\u003c\/p\u003e \u003cp\u003e8.11 Home\/Class Work 8.3 (Air Compression)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh9. The Optimization Tool\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e9.1 Problem Description: Defining the Objective Function\u003c\/p\u003e \u003cp\u003e9.2 The Property Method: “STEAMNBS”\u003c\/p\u003e \u003cp\u003e9.3 A Flowsheet for Water Transport\u003c\/p\u003e \u003cp\u003e9.4 Entering Stream, Pump, and Pipe Specifications\u003c\/p\u003e \u003cp\u003e9.5 Model Analysis Tools: The Optimization Tool\u003c\/p\u003e \u003cp\u003e9.6 Model Analysis Tools: The Sensitivity Tool\u003c\/p\u003e \u003cp\u003e9.7 Last Comments\u003c\/p\u003e \u003cp\u003e9.8 References\u003c\/p\u003e \u003cp\u003e9.9 Home\/Class Work 9.1 (Swamee-Jain Equation)\u003c\/p\u003e \u003cp\u003e9.10 Home\/Class Work 9.2 (A Simplified Pipe Diameter Optimization)\u003c\/p\u003e \u003cp\u003e9.11 Home\/Class Work 9.3 (The Optimum Diameter for a Viscous Flow)\u003c\/p\u003e \u003cp\u003e9.12 Home\/Class Work 9.4 (The Selectivity of Parallel Reactions)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh10. Heat Exchanger (H.E.) Design\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e10.1 Problem Description\u003c\/p\u003e \u003cp\u003e10.2 Types of Heat Exchanger Models in Aspen Plus\u003c\/p\u003e \u003cp\u003e10.3 The Simple Heat Exchanger Model (“Heater”)\u003c\/p\u003e \u003cp\u003e10.4 The Rigorous Heat Exchanger Model (“HeatX”)\u003c\/p\u003e \u003cp\u003e10.5 The Rigorous Exchanger Design and Rating (EDR) Procedure\u003c\/p\u003e \u003cp\u003e10.5.1 The EDR Exchanger Feasibility Panel\u003c\/p\u003e \u003cp\u003e10.5.2 The Rigorous Mode within the “HeatX” Block\u003c\/p\u003e \u003cp\u003e10.6 General Footnotes on EDR Exchanger\u003c\/p\u003e \u003cp\u003e10.7 References\u003c\/p\u003e \u003cp\u003e10.8 Home\/Class Work 10.1 (Heat Exchanger with Phase Change)\u003c\/p\u003e \u003cp\u003e10.9 Home\/Class Work 10.2 (High Heat Duty Heat Exchanger)\u003c\/p\u003e \u003cp\u003e10.10 Home\/Class Work 10.3 (Design Spec Heat Exchanger)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh11. Electrolytes\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e11.1 Problem Description: Water De-Souring\u003c\/p\u003e \u003cp\u003e11.2 What is an Electrolyte?\u003c\/p\u003e \u003cp\u003e11.3 The Property Method for Electrolytes\u003c\/p\u003e \u003cp\u003e11.4 The Electrolyte Wizard\u003c\/p\u003e \u003cp\u003e11.5 Water De-Souring Process Flowsheet\u003c\/p\u003e \u003cp\u003e11.6 Entering the Specifications of Feed Streams and the Stripper\u003c\/p\u003e \u003cp\u003e11.7 Appendix: Development of “ELECNRTL” Model\u003c\/p\u003e \u003cp\u003e11.8 References\u003c\/p\u003e \u003cp\u003e11.9 Home\/Class Work 11.1 (An Acidic Sludge Neutralization)\u003c\/p\u003e \u003cp\u003e11.10 Home\/Class Work 11.2 (CO2 Removal from Natural Gas)\u003c\/p\u003e \u003cp\u003e11.11 Home\/Class Work 11.3 (pH of Aqueous Solutions of Salts)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh12. Polymerization Processes\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e12.1 The Theoretical Background\u003c\/p\u003e \u003cp\u003e12.1.1 Polymerization Reactions\u003c\/p\u003e \u003cp\u003e12.1.2 Catalyst Types\u003c\/p\u003e \u003cp\u003e12.1.3 Ethylene Process Types\u003c\/p\u003e \u003cp\u003e12.1.4 Reaction Kinetic Scheme\u003c\/p\u003e \u003cp\u003e12.1.5 Reaction Steps\u003c\/p\u003e \u003cp\u003e12.1.6 Catalyst States\u003c\/p\u003e \u003cp\u003e12.2 High-Density Poly-Ethylene (HDPE) High Temperature Solution Process\u003c\/p\u003e \u003cp\u003e12.2.1 Problem Definition\u003c\/p\u003e \u003cp\u003e12.2.2 Process Conditions\u003c\/p\u003e \u003cp\u003e12.3 Creating Aspen Plus Flowsheet for HDPE\u003c\/p\u003e \u003cp\u003e12.4 Improving Convergence\u003c\/p\u003e \u003cp\u003e12.5 Presenting the Property Distribution of Polymer\u003c\/p\u003e \u003cp\u003e12.6 Home\/Class Work 12.1 (Maximizing the Degree of HDPE Polymerization)\u003c\/p\u003e \u003cp\u003e12.7 Home\/Class Work 12.2 (Styrene Acrylo-Nitrile (SAN) Polymerization)\u003c\/p\u003e \u003cp\u003e12.8 References\u003c\/p\u003e \u003cp\u003e12.9 Appendix A: The Main Features \u0026amp; Assumptions of Aspen Plus Chain Polymerization Model\u003c\/p\u003e \u003cp\u003e12.9.1 Polymerization Mechanism\u003c\/p\u003e \u003cp\u003e12.9.2 Co-polymerization Mechanism\u003c\/p\u003e \u003cp\u003e12.9.3 Rate Expressions\u003c\/p\u003e \u003cp\u003e12.9.4 Rate Constants\u003c\/p\u003e \u003cp\u003e12.9.5 Catalyst Pre-Activation\u003c\/p\u003e \u003cp\u003e12.9.6 Catalyst Site Activation\u003c\/p\u003e \u003cp\u003e12.9.7 Site Activation Reactions\u003c\/p\u003e \u003cp\u003e12.9.8 Chain Initiation\u003c\/p\u003e \u003cp\u003e12.9.9 Propagation\u003c\/p\u003e \u003cp\u003e12.9.10 Chain Transfer to Small Molecules\u003c\/p\u003e \u003cp\u003e12.9.11 Chain Transfer to Monomer\u003c\/p\u003e \u003cp\u003e12.9.12 Site Deactivation\u003c\/p\u003e \u003cp\u003e12.9.13 Site Inhibition\u003c\/p\u003e \u003cp\u003e12.9.14 Co-Catalyst Poisoning\u003c\/p\u003e \u003cp\u003e12.9.15 Terminal Double Bond Polymerization\u003c\/p\u003e \u003cp\u003e12.9.16 Phase Equilibria\u003c\/p\u003e \u003cp\u003e12.9.17 Rate Calculations\u003c\/p\u003e \u003cp\u003e12.9.18 Calculated Polymer Properties\u003c\/p\u003e \u003cp\u003e12.10 Appendix B: The Number Average Molecular Weight (MWN) and Weight Average Molecular Weight (MWW)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh13. Characterization of Drug-Like Molecules Using Aspen Properties\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e13.1 Introduction\u003c\/p\u003e \u003cp\u003e13.2 Problem Description\u003c\/p\u003e \u003cp\u003e13.3 Creating Aspen Plus Pharmaceutical Template\u003c\/p\u003e \u003cp\u003e13.3.1 Entering the User-Defined Benzamide (BNZMD-UD) as Conventional\u003c\/p\u003e \u003cp\u003e13.3.2 Specifying Properties to Estimate\u003c\/p\u003e \u003cp\u003e13.4 Defining Molecular Structure of BNZMD-UD\u003c\/p\u003e \u003cp\u003e13.5 Entering Property Data\u003c\/p\u003e \u003cp\u003e13.6 Contrasting Aspen Plus Databank (BNZMD-DB) versus BNZMD-UD\u003c\/p\u003e \u003cp\u003e13.7 References\u003c\/p\u003e \u003cp\u003e13.8 Home\/Class Work 13.1 (Vanillin)\u003c\/p\u003e \u003cp\u003e13.9 Home\/Class Work 13.2 (Ibuprofen)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh14. Solids Handling\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e14.1 Introduction\u003c\/p\u003e \u003cp\u003e14.2 Problem Description #1: The Crusher\u003c\/p\u003e \u003cp\u003e14.3 Creating Aspen Plus Flowsheet\u003c\/p\u003e \u003cp\u003e14.3.1 Entering Components Information\u003c\/p\u003e \u003cp\u003e14.3.2 Adding the Flowsheet Objects\u003c\/p\u003e \u003cp\u003e14.3.3 Defining the Particle Size Distribution (PSD)\u003c\/p\u003e \u003cp\u003e14.3.4 Calculation of the Outlet PSD\u003c\/p\u003e \u003cp\u003e14.4 Exercise 14.1: (Determine Crusher Outlet PSD from Comminution Power)\u003c\/p\u003e \u003cp\u003e14.5 Exercise 14.2: (Specifying Crusher Outlet PSD)\u003c\/p\u003e \u003cp\u003e14.6 Problem Description #2: The Fluidized Bed for Alumina Dehydration\u003c\/p\u003e \u003cp\u003e14.7 Creating Aspen Plus Flowsheet\u003c\/p\u003e \u003cp\u003e14.7.1 Entering Components Information\u003c\/p\u003e \u003cp\u003e14.7.2 Adding the Flowsheet Objects\u003c\/p\u003e \u003cp\u003e14.7.3 Entering Input Data\u003c\/p\u003e \u003cp\u003e14.7.4 Results\u003c\/p\u003e \u003cp\u003e14.8 Exercise 14.3: (Re-Converging the Solution for an Input Change)\u003c\/p\u003e \u003cp\u003e14.9 References\u003c\/p\u003e \u003cp\u003e14.10 Home\/Class Work 14.1 (KCl Drying)\u003c\/p\u003e \u003cp\u003e14.11 Home\/Class Work 14.2 (KCl Crystallization)\u003c\/p\u003e \u003cp\u003e14.12 APPENDIX A: Solids Unit Operations\u003c\/p\u003e \u003cp\u003e14.12.1 Unit Operation Solids Models\u003c\/p\u003e \u003cp\u003e14.12.2 Solids Separators Models\u003c\/p\u003e \u003cp\u003e14.12.3 Solids Handling Models\u003c\/p\u003e \u003cp\u003e14.13 APPENDIX B: Solids Classification\u003c\/p\u003e \u003cp\u003e14.14 APPENDIX C: Predefined Stream Classification\u003c\/p\u003e \u003cp\u003e14.15 APPENDIX D: Substream Classes\u003c\/p\u003e \u003cp\u003e14.16 APPENDIX E: Particle Size Distribution (PSD)\u003c\/p\u003e \u003cp\u003e14.17 APPENDIX F: Fluidized Beds\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh15. Aspen Plus Dynamics\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e15.1 Introduction\u003c\/p\u003e \u003cp\u003e15.2 Problem Description\u003c\/p\u003e \u003cp\u003e15.3 Preparing Aspen Plus Simulation for Aspen Plus Dynamics (APD)\u003c\/p\u003e \u003cp\u003e15.4 Conversion of Aspen Plus Steady-State into Dynamic Simulation\u003c\/p\u003e \u003cp\u003e15.4.1 Modes of Dynamic CSTR Heat Transfer\u003c\/p\u003e \u003cp\u003e15.4.2 Creating Pressure-Driven Dynamic Files for APD\u003c\/p\u003e \u003cp\u003e15.5 Opening a Dynamic File Using APD\u003c\/p\u003e \u003cp\u003e15.6 The “Simulation Messages” Window\u003c\/p\u003e \u003cp\u003e15.7 The Running Mode: Initialization\u003c\/p\u003e \u003cp\u003e15.8 Adding Temperature Control (TC) Unit\u003c\/p\u003e \u003cp\u003e15.9 Snapshots Management for Captured Successful Old Runs\u003c\/p\u003e \u003cp\u003e15.10 The Controller Faceplate\u003c\/p\u003e \u003cp\u003e15.11 Communication Time for Updating\/Presenting Results\u003c\/p\u003e \u003cp\u003e15.12 The Closed-Loop Auto-Tune Variation (ATV) Test versus Open-Loop Tune-Up Test\u003c\/p\u003e \u003cp\u003e15.13 The Open-Loop (Manual Mode) Tune-Up for Liquid Level Controller\u003c\/p\u003e \u003cp\u003e15.14 The Closed-Loop Dynamic Response for Liquid Level Load Disturbance\u003c\/p\u003e \u003cp\u003e15.15 The Closed-Loop Dynamic Response for Liquid Level Set-Point Disturbance\u003c\/p\u003e \u003cp\u003e15.16 Accounting for Dead\/Lag Time in Process Dynamics\u003c\/p\u003e \u003cp\u003e15.17 The Closed-Loop (Auto Mode) ATV Test for Temperature Controller (TC)\u003c\/p\u003e \u003cp\u003e15.18 The Closed-Loop Dynamic Response: “TC” Response to Temperature Load Disturbance\u003c\/p\u003e \u003cp\u003e15.19 Interactions between “LC” and “TC” Control Unit\u003c\/p\u003e \u003cp\u003e15.20 The Stability of a Process without Control\u003c\/p\u003e \u003cp\u003e15.21 The Cascade Control\u003c\/p\u003e \u003cp\u003e15.22 Monitoring of Variables as Functions of Time\u003c\/p\u003e \u003cp\u003e15.23 Final Notes on the Virtual (Dry) Process Control in APD\u003c\/p\u003e \u003cp\u003e15.24 References\u003c\/p\u003e \u003cp\u003e15.25 Home\/Class Work 15.1 (A Cascade Control of a Simple Water Heater)\u003c\/p\u003e \u003cp\u003e15.26 Home\/Class Work 15.2 (A CSTR Control with “LMTD” Heat Transfer Option)\u003c\/p\u003e \u003cp\u003e15.27 Home\/Class Work 15.3 (A PFR Control for Ethyl-Benzene Production)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh16. Safety \u0026amp; Energy Aspects of Chemical Processes\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e16.1 Introduction\u003c\/p\u003e \u003cp\u003e16.2 Problem Description\u003c\/p\u003e \u003cp\u003e16.3 The “Safety Analysis” Environment\u003c\/p\u003e \u003cp\u003e16.4 Adding a Pressure Safety Valve (PSV)\u003c\/p\u003e \u003cp\u003e16.5 Adding a Rupture Disk (RD)\u003c\/p\u003e \u003cp\u003e16.6 Presentation of Safety-Related Documents\u003c\/p\u003e \u003cp\u003e16.7 Preparation of Flowsheet for “Energy Analysis” Environment\u003c\/p\u003e \u003cp\u003e16.8 The “Energy Analysis” Activation\u003c\/p\u003e \u003cp\u003e16.9 The “Energy Analysis” Environment\u003c\/p\u003e \u003cp\u003e16.10 The Aspen Energy Analyzer\u003c\/p\u003e \u003cp\u003e16.11 Home\/Class Work 16.1 (Adding a Storage Tank Protection)\u003c\/p\u003e \u003cp\u003e16.12 Home\/Class Work 16.2 (Separation of C2\/C3\/C4 Hydrocarbon Mixture)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh17. Aspen Process Economic Analyzer (APEA)\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e17.1 Optimized Process Flowsheet for Acetic Anhydride Production\u003c\/p\u003e \u003cp\u003e17.2 Costing Options in Aspen Plus\u003c\/p\u003e \u003cp\u003e17.2.1 Aspen Process Economic Analyzer (APEA) Estimation Template\u003c\/p\u003e \u003cp\u003e17.2.2 Feed and Product Stream Prices\u003c\/p\u003e \u003cp\u003e17.2.3 Utility Association with a Flowsheet Block\u003c\/p\u003e \u003cp\u003e17.3 The First Route for Chemical Process Costing\u003c\/p\u003e \u003cp\u003e17.4 The Second Route for Chemical Process Costing\u003c\/p\u003e \u003cp\u003e17.4.1 Project Properties\u003c\/p\u003e \u003cp\u003e17.4.2 Loading Simulator Data\u003c\/p\u003e \u003cp\u003e17.4.3 Mapping and Sizing\u003c\/p\u003e \u003cp\u003e17.4.4 Project Evaluation\u003c\/p\u003e \u003cp\u003e17.4.5 Fixing Geometrical Design-Related Errors\u003c\/p\u003e \u003cp\u003e17.4.6 Executive Summary\u003c\/p\u003e \u003cp\u003e17.4.7 Capital Costs Report\u003c\/p\u003e \u003cp\u003e17.4.8 Investment Analysis\u003c\/p\u003e \u003cp\u003e17.5 Home\/Class Work 17.1 (Feed\/Product Unit Price Effect on Process Profitability)\u003c\/p\u003e \u003cp\u003e17.6 Home\/Class Work 17.2 (Using European Economic Template)\u003c\/p\u003e \u003cp\u003e17.7 Home\/Class Work 17.3 (Process Profitability of Acetone Recovery from Spent Solvent)\u003c\/p\u003e \u003cp\u003e17.8 Appendix\u003c\/p\u003e \u003cp\u003e17.8.1 Net Present Value (NPV) for a Chemical Process Plant\u003c\/p\u003e \u003cp\u003e17.8.2 Discounted Payout (Payback) Period (DPP)\u003c\/p\u003e \u003cp\u003e17.8.3 Profitability Index\u003c\/p\u003e \u003cp\u003e17.8.4 Internal Rate of Return (IRR)\u003c\/p\u003e \u003cp\u003e17.8.5 Modified Internal Rate of Return (MIRR)\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh18. \u003cb\u003eTerm Projects (TP) \u003c\/b\u003e\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e18.1 What is Aspen Custom Modeler\u003c\/p\u003e \u003cp\u003e18.2 Main Feature of ACM\u003c\/p\u003e \u003cp\u003e18.3 Modeling and Simulation of a Simple Constant-Temperature Mixing Tank\u003c\/p\u003e \u003cp\u003e18.4 Modeling and Simulation of a non-Isothermal Mixing Tank\u003c\/p\u003e \u003cp\u003e18.5 Modeling and Simulation of a Flash Drum\u003c\/p\u003e \u003cp\u003e18.6 Modeling and Simulation of Heat Slab\u003c\/p\u003e \u003cp\u003e18.7 Modeling and Simulation of an Absorber\u003c\/p\u003e \u003cp\u003e18.8 Modeling and Simulation of a Jacketed Reactor\u003c\/p\u003e \u003cp\u003e18.9 Modeling and Simulation of a Heat Exchanger\u003c\/p\u003e \u003cp\u003e18.10 Merging of ACM models into AP Model Palette\u003c\/p\u003e \u003cp\u003e\u003cb\u003eCh19. \u003cb\u003eAspen Custom Modeler (ACM)\u003c\/b\u003e\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e19.1 TP #1: Production of Acetone via the Dehydration of Iso-Propanol\u003c\/p\u003e \u003cp\u003e19.2 TP #2: Production of Formaldehyde from Methanol (Sensitivity Analysis)\u003c\/p\u003e \u003cp\u003e19.3 TP #3: Production of Di-Methyl Ether (Process Economics \u0026amp; Control)\u003c\/p\u003e \u003cp\u003e18.3.1 Economic Analysis\u003c\/p\u003e \u003cp\u003e18.3.2 Process Dynamics \u0026amp; Control\u003c\/p\u003e \u003cp\u003e19.4 TP #4: Production of Acetic Acid via Partial Oxidation of Ethylene Gas\u003c\/p\u003e \u003cp\u003e19.5 TP #5: Pyrolysis of Benzene\u003c\/p\u003e \u003cp\u003e19.6 TP #6: Re-Use of Spent Solvents\u003c\/p\u003e \u003cp\u003e19.7 TP#7: Solids Handling: Production of Potassium Sulfate from Sodium Sulfate\u003c\/p\u003e \u003cp\u003e19.8 TP #8: Solids Handling: Production of CaCO3-Based Agglomerate as a General Additive\u003c\/p\u003e \u003cp\u003e19.9 TP #9: Solids Handling: Formulation of Di-Ammonium Phosphate and Potassium Nitrate Blend Fertilizer\u003c\/p\u003e \u003cp\u003e19.10 TP #10: “Flowsheeting Options” | “Calculator”: Gas De-Souring and Sweetening Process\u003c\/p\u003e \u003cp\u003e19.11 TP #11: Using More Than One Property Method and Stream Class: Solid Catalyzed Direct Hydration of Propylene to Iso-Propyl Alcohol (IPA)\u003c\/p\u003e \u003cp\u003e19.12 TP #12: Polymerization: Production of Poly-Vinyl Acetate (PVAC)\u003c\/p\u003e \u003cp\u003e19.13 TP #13: Polymerization: Emulsion Copolymerization of Styrene and Butadiene to Produce SBR\u003c\/p\u003e \u003cp\u003e19.14 TP #14: Polymerization: Free Radical Polymerization of Methyl-Methacrylate to Produce Poly (Methyl Methacrylate)\u003c\/p\u003e \u003cp\u003e19.15 TP #15: LHHW Kinetics: Production of Cyclo-Hexanone-Oxime (CYCHXOXM) via Cyclo-Hexanone Ammoximation Using Clay-Based Titanium Silicalite (TS) Catalyst\u003c\/p\u003e  \u003cp\u003e\u003cb\u003eKamal I. M. Al-Malah\u003c\/b\u003e received his PhD degree from Oregon State University in 1993. He served as a Professor of Chemical Engineering in Jordan and other Gulf countries, as well as Former Chairman of the Chemical Engineering Department at the University of Hail in Saudi Arabia. Professor Al-Malah is an expert in both Aspen Plus\u003csup\u003e®\u003c\/sup\u003e and MATLAB\u003csup\u003e®\u003c\/sup\u003e applications. He has created a bundle of Windows-based software for engineering applications.   \u003c\/p\u003e\u003cp\u003e\u003cb\u003eComprehensive resource covering Aspen Plus V12.1 and demonstrating how to implement the program in versatile chemical process industries\u003c\/b\u003e \u003c\/p\u003e\u003cp\u003e\u003ci\u003eAspen Plus\u003csup\u003e®\u003c\/sup\u003e: Chemical Engineering Applications\u003c\/i\u003e facilitates the process of learning and later mastering Aspen Plus\u003csup\u003e®\u003c\/sup\u003e, the market-leading chemical process modeling software, with step-by-step examples and succinct explanations. The text enables readers to identify solutions to various process engineering problems via screenshots of the Aspen Plus\u003csup\u003e®\u003c\/sup\u003e platforms in parallel with the related text. \u003c\/p\u003e\u003cp\u003eTo aid in information retention, the text includes end-of-chapter problems and term project problems, online exam and quiz problems for instructors that are parametrized (i.e., adjustable) so that each student will have a standalone version, and extra online material for students, such as Aspen Plus\u003csup\u003e®\u003c\/sup\u003e-related files, that are used in the working tutorials throughout the entire textbook. \u003c\/p\u003e\u003cp\u003eThe second edition of \u003ci\u003eAspen Plus\u003c\/i\u003e\u003csup\u003e®\u003c\/sup\u003e: \u003ci\u003eChemical Engineering Applications\u003c\/i\u003e includes information on: \u003c\/p\u003e\u003cul\u003e\n\u003cli\u003eVarious new features that were embedded into Aspen Plus V12.1 and existing features which have been modified\u003c\/li\u003e \u003cli\u003eAspen Custom Modeler (ACM), covering basic features to show how to merge customized models into Aspen Plus simulator\u003c\/li\u003e \u003cli\u003eNew updates to process dynamics and control and process economic analysis since the first edition was published\u003c\/li\u003e \u003cli\u003eVital areas of interest in relation to the software, such as polymerization, drug solubility, solids handling, safety measures, and energy saving \u003c\/li\u003e\n\u003c\/ul\u003e \u003cp\u003eFor chemical engineering students and industry professionals, the second edition of \u003ci\u003eAspen Plus\u003csup\u003e®\u003c\/sup\u003e: Chemical Engineering Applications\u003c\/i\u003e is a key resource for understanding Aspen Plus and the new features that were added in version 12.1 of the software. Many supplementary learning resources help aid the reader with information retention.\u003c\/p\u003e","brand":"Wiley","offers":[{"title":"Default Title","offer_id":47988767981797,"sku":"NP9781119868699","price":127.0,"currency_code":"USD","in_stock":false}],"thumbnail_url":"\/\/cdn.shopify.com\/s\/files\/1\/1842\/7735\/files\/9781119868699.jpg?v=1761781516","url":"https:\/\/k12savings.com\/products\/aspen-plus-isbn-9781119868699","provider":"K12savings","version":"1.0","type":"link"}