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Hameed

Chemical Process Simulations Using Aspen Hysys

Medium: Buch
ISBN: 978-1-394-29327-8
Verlag: Wiley
Erscheinungstermin: 28.05.2025
Lieferfrist: bis zu 10 Tage

An intuitive guide to using Aspen HYSYS for chemical, petrochemical, and petroleum industry process simulations, including interactive process flow diagrams

In Chemical Process Simulations using Aspen Hysys, distinguished lecturer Dr. Khalid W. Hameed delivers an up-to-date and authoritative discussion of the simulation and design of chemical, petrochemical, and petroleum industry processes using Aspen HYSYS. The book includes coverage of many chemical engineering topics including fluid flow, reactors, unit operation of heat and mass transfer, oil refinery process, and control systems.

Readers will also find highly interactive process flow diagrams for building and navigating through large simulations, as well as: - A thorough introduction to the use of Aspen HYSYS for the chemical, oil, and petrochemical industries
- Skill development techniques for users of Aspen HYSYS and strategies for improving the accuracy of results

- Practical discussions of Dynamic State Simulation with explanations of how to install control systems for the process using flash separator, gas processing, and advanced process control such as ratio control, cascade control, and split range control
- Illustrative examples of Plant Wide Projects that demonstrate the ability of Aspen HYSYS to perform a full plant

Perfect for research and development engineers in the fields of petrochemical, chemical, and petroleum engineering, Chemical Process Simulations using Aspen HYSYS will also benefit researchers with an interest in the area.


Produkteigenschaften


  • Artikelnummer: 9781394293278
  • Medium: Buch
  • ISBN: 978-1-394-29327-8
  • Verlag: Wiley
  • Erscheinungstermin: 28.05.2025
  • Sprache(n): Englisch
  • Auflage: 1. Auflage 2025
  • Produktform: Gebunden
  • Seiten: 528
  • Ausgabetyp: Kein, Unbekannt
Autoren/Hrsg.

Autoren

Preface xv

Acknowledgments xix

1 Starting with Aspen HYSYS 1

1.1 HYSYS Menu Command to Ribbon Map 2

1.2 Starting Aspen HYSYS 7

1.3 Properties Environment 8

1.4 Creation of a New Simulation 8

1.5 Inserting Components to the Simulation 8

1.6 Adding the Fluid Package 10

1.7 Methods for Choosing Thermodynamics Model (Fluid Package) 11

1.8 Simulation Environment 15

1.9 Creating Material Streams 16

1.10 Summary 21

1.11 Printing 22

2 Physical and Thermodynamics Properties 25

2.1 Fluid Package 25

2.2 Steam Table 36

2.3 Bubble-Point and Dew-Point Calculations 38

2.4 Humidity Calculations 41

3 Pressure Change Equipment 47

3.1 Pump 47

3.2 Expander 53

3.3 Compressor 57

4 Heating and Cooling 65

4.1 Heat Exchanger 65

4.2 Air Cooler 73

4.3 Fired Heater 78

4.4 Summary 89

5 Flash Separator 93

5.1 Simulation of Flash Separator 94

5.2 Simulation of Evaporator 100

6 Logical Operations 113

6.1 Set Operation 113

6.2 Adjust Operation 114

6.3 Balance 117

6.4 Recycle 121

6.5 Spreadsheet 122

7 Piping Equipment 125

7.1 Pipe Segment 125

7.2 PIPESYS 135

7.3 Sizing of Pressure Relieve Valve 153

7.4 Summary 159

8 Reactors161

8.1 Reactor Types 161

8.2 Parameters in the Reactors 163

8.3 Conversion Reactor 164

8.4 Equilibrium Reactor 171

8.5 Miscellaneous Examples 179

8.6 CSTR (Continuous Stirred Tank Reactor) 198

8.7 Plug Flow Reactor 205

8.8 Gibbs Reactor 218

9 Separation Columns 231

9.1 Absorption Column 231

9.2 Gas Desorption (Stripping) 241

9.3 Distillation Column 241

9.4 Extraction Column 267

9.5 Miscellaneous Examples 273

10 Refinery Process 321

10.1 Refinery of Crude Oil 321

10.2 Simulation of Refinery Process 330

10.3 Summary 373

11 Optimizer 375

11.1 Simple Optimizer 375

11.2 Original Optimizer 383

11.3 Summary 388

12 Solid Operation 389

12.1 Cyclone 389

12.2 Rotary Vacuum Filter 398

12.3 Baghouse Filter 402

13 Dynamic-State Simulation 411

13.1 Problem Statement 1: Flash Separator 411

13.2 Problem Statement 2: Gas Processing 425

13.3 Advanced Control 445

13.4 Summary 467

14 Economic Evaluation 471

14.1 Problem Statement 471

14.2 Simulation 471

14.3 Summary 481

15 Plant-Wide Projects 483

15.1 Cyclohexane Production Plant 483

15.2 Production of Dimethyl_ether 486

15.3 Gas Sweetening 488

15.4 Propylene Production 490

15.5 Methanol Production 492

15.6 Production of Vinyl_Chloride_Monomer 494

References 496

Index 499