Aspen Plus : chemical engineering applications /: chemical engineering applications. (2022)

• Record Type: Book
• Further Information: Note: Kamal I.M. Al-Malah.
• Authors: Al-Malah, Kamal I. M
• Contents: Ch1. Introducing Aspen Plus 1.1 What does ASPEN stand for? 1.2 What is Aspen Plus Process Simulation Model? 1.3 Launching Aspen Plus V12.0 1.4 Beginning a Simulation 1.5 Entering Components 1.6 Specifying the Property Method 1.7 Improvement of the Property Method Accuracy 1.8 File Saving 1.9 Exercise 1.1 1.10 Good Flowsheeting Practice 1.11 Aspen Plus Built-in Help 1.12 For More Information 1.13 Home/Class Work 1.1 (Pxy) 1.14 Home/Class Work 1.2 (Gmix) 1.15 Home/Class Work 1.3 (Likes Dissolve Likes) as Envisaged by NRTL Property Method 1.16 Home/Class Work 1.4 (The Mixing Rule) Ch2. More on Aspen Plus Flowsheet Features (1) 2.1 Problem Description 2.2 Entering and Naming Compounds 2.3 Binary Interactions 2.4 The “Simulation” Environment: Activation Dashboard 2.5 Placing a Block and Material Stream from Model Palette 2.6 Block and Stream Manipulation 2.7 Data Input, Project Title, & Report Options 2.8 Running the Simulation 2.9 The Difference among Recommended Property Methods 2.10 NIST/TDE Experimental Data 2.11 Home-/Class-Work 2.1 (Water-Alcohol System) 2.12 Home-/Class-Work 2.2 (Water-Acetone-EIPK System with NIST/DTE Data) 2.13 Home-/Class-Work 2.3 (Water-Acetone-EIPK System without NIST/DTE Data) Ch3. More on Aspen Plus Flowsheet Features (2) 3.1 Problem Description: Continuation to Chapter Two Problem 3.2 The Clean Parameters Step 3.3 Simulation Results Convergence 3.4 Adding Stream Table 3.5 Property Sets 3.6 Adding Stream Conditions 3.7 Printing from Aspen Plus 3.8 Viewing the Input Summary 3.9 Report Generation 3.10 Stream Properties 3.11 Adding a Flash Separation Unit 3.12 The Required Input for “Flash3”-Type Separator 3.13 Running the Simulation and Checking the Results 3.14 Home-/Class-Work 3.1 (Output of Input Data & Results) 3.15 Home-/Class-Work 3.2 (Output of Input Data & Results) 3.16 Home-/Class-Work 3.3 (Output of Input Data & Results) 3.17 Home-/Class-Work 3.4 (The Partition Coefficient of a Solute) Ch4. Flash Separation & Distillation Columns 4.1 Problem Description 4.2 Adding a Second Mixer and Flash 4.3 Design Specifications Study 4.4 Exercise 4.1 (Design Spec) 4.5 Aspen Plus Distillation Column Options 4.6 “DSTWU” Distillation Column 4.7 “Distl” Distillation column 4.8 “RadFrac” Distillation Column 4.9 Home/Class Work 4.1 (Water-Alcohol System) 4.10 Home/Class Work 4.2 (Water-Acetone-EIPK System with NIST/DTE Data) 4.11 Home/Class Work 4.2 (Water-Acetone-EIPK System without NIST/DTE Data) 4.12 Home/Class Work 4.4 (Scrubber) Ch5. Liquid-Liquid Extraction Process 5.1 Problem Description 5.2 The Proper Selection for Property Method for Extraction Processes 5.3 Defining New Property Sets 5.4 Property Method Validation versus Experimental Data Using Sensitivity Analysis 5.5 A Multi-Stage Extraction Column 5.6 The Triangle Diagram 5.7 References 5.8 Home/Class Work 5.1 (Separation of MEK from Octanol) 5.9 Home/Class Work 5.2 (Separation of MEK from Water Using Octane) 5.10 Home/Class Work 5.3 (Separation of Acetic Acid from Water Using Iso-Propyl Butyl Ether) 5.11 Home/Class Work 5.4 (Separation of Acetone from Water Using Tri-Chloro-Ethane) 5.12 Home/Class Work 5.5 (Separation of Propionic Acid from Water Using MEK) Ch6. Reactors with Simple Reaction Kinetic Forms 6.1 Problem Description 6.2 Defining Reaction Rate Constant to Aspen Plus Environment 6.3 Entering Components and Method of Property 6.4 The Rigorous Plug Flow Reactor (RPLUG) 6.5 Reactor and Reaction Specifications for RPLUG (PFR) 6.6 Running the Simulation (PFR Only) 6.7 Exercise 6.1 6.8 Compressor (CMPRSSR) and RadFrac Rectifying Column (RECTIF) 6.9 Running the Simulation (PFR + CMPRSSR + RECTIF) 6.10 Exercise 6.2 6.11 RadFrac Distillation Column (DSTL) 6.12 Running the Simulation (PFR + CMPRSSR + RECTIF+DSTL) 6.13 Reactor and Reaction Specifications for RCSTR 6.14 Running the Simulation (PFR + CMPRSSR + RECTIF+DSTL+RCSTR) 6.15 Exercise 6.3 6.16 Sensitivity Analysis: The Reactor’s Optimum Operating Conditions 6.17 References 6.18 Home/Class Work 6.1 (Hydrogen Peroxide Shelf-Life) 6.19 Home/Class Work 6.2 (Esterification Process) 6.20 Home/Class Work 6.3 (Liquid-Phase Isomerization of n-Butane) Ch7. Reactors with Complex (Non-Conventional) Reaction Kinetic Forms 7.1 Problem Description 7.2 Non-Conventional Kinetics: LHHW Type Reaction 7.3 General Expressions for Specifying LHHW Type Reaction in Aspen Plus 7.3.1 The “Driving Force” for the Non-Reversible (Irreversible) Case 7.3.2 The “Driving Force” for the Reversible Case 7.3.3 The “Adsorption Expression” 7.4 The Property Method: “SRK” 7.5 RPLUG Flowsheet for Methanol Production 7.6 Entering Input Parameters 7.7 Defining Methanol Production Reactions as LHHW Type 7.8 Sensitivity Analysis: Effect of Temperature and Pressure on Selectivity 7.9 References 7.10 Home/Class Work 7.1 (Gas-Phase Oxidation of Chloroform) 7.11 Home/Class Work 7.2 (Formation of Styrene from Ethyl-Benzene) 7.12 Home/Class Work 7.3 (Combustion of Methane over Steam-Aged Pt-Pd Catalyst) Ch8. Pressure Drop, Friction Factor, NPSHA, and Cavitation 8.1 Problem Description 8.2 The Property Method: “STEAMNBS” 8.3 A Water Pumping Flowsheet 8.4 Entering Pipe, Pump, & Fittings Specifications 8.5 Results: Frictional Pressure Drop, the Pump Work, Valve Choking, and ANPSH versus RNPSH 8.6 Exercise 8.1 8.7 Model Analysis Tools: Sensitivity for the Onset of Cavitation or Valve Choking Condition 8.8 References 8.9 Home/Class Work 8.1 (Pentane Transport) 8.10 Home/Class Work 8.2 (Glycerol Transport) 8.11 Home/Class Work 8.3 (Air Compression) Ch9. The Optimization Tool 9.1 Problem Description: Defining the Objective Function 9.2 The Property Method: “STEAMNBS” 9.3 A Flowsheet for Water Transport 9.4 Entering Stream, Pump, and Pipe Specifications 9.5 Model Analysis Tools: The Optimization Tool 9.6 Model Analysis Tools: The Sensitivity Tool 9.7 Last Comments 9.8 References 9.9 Home/Class Work 9.1 (Swamee-Jain Equation) 9.10 Home/Class Work 9.2 (A Simplified Pipe Diameter Optimization) 9.11 Home/Class Work 9.3 (The Optimum Diameter for a Viscous Flow) 9.12 Home/Class Work 9.4 (The Selectivity of Parallel Reactions) Ch10. Heat Exchanger (H.E.) Design 10.1 Problem Description 10.2 Types of Heat Exchanger Models in Aspen Plus 10.3 The Simple Heat Exchanger Model (“Heater”) 10.4 The Rigorous Heat Exchanger Model (“HeatX”) 10.5 The Rigorous Exchanger Design and Rating (EDR) Procedure 10.5.1 The EDR Exchanger Feasibility Panel 10.5.2 The Rigorous Mode within the “HeatX” Block 10.6 General Footnotes on EDR Exchanger 10.7 References 10.8 Home/Class Work 10.1 (Heat Exchanger with Phase Change) 10.9 Home/Class Work 10.2 (High Heat Duty Heat Exchanger) 10.10 Home/Class Work 10.3 (Design Spec Heat Exchanger) Ch11. Electrolytes 11.1 Problem Description: Water De-Souring 11.2 What is an Electrolyte? &lt
• Edition: Second edition
• Publisher Details: Hoboken : John Wiley & Sons, Inc
• Publication Date: 2022
• Extent: 1 online resource
• Subjects: 660.28; Chemical processes -- Computer simulation; Chemical process control -- Computer programs
• Languages: English
• ISBNs: 9781119868712
• Notes: Note: Description based on CIP data; resource not viewed.
• Access Rights: Legal Deposit; Only available on premises controlled by the deposit library and to one user at any one time; The Legal Deposit Libraries (Non-Print Works) Regulations (UK).
• Access Usage: Restricted: Printing from this resource is governed by The Legal Deposit Libraries (Non-Print Works) Regulations (UK) and UK copyright law currently in force.