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E-raamat: Teach Yourself the Basics of Aspen Plus

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  • Ilmumisaeg: 13-Sep-2016
  • Kirjastus: Wiley-AIChE
  • Keel: eng
  • ISBN-13: 9781119276449
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  • Formaat: PDF+DRM
  • Ilmumisaeg: 13-Sep-2016
  • Kirjastus: Wiley-AIChE
  • Keel: eng
  • ISBN-13: 9781119276449

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The complete step-by-step guide to mastering the basics of Aspen Plus software

Used for a wide variety of important scientific tasks, Aspen Plus software is a modeling tool used for conceptual design, optimization, and performance monitoring of chemical processes. After more than twenty years, it remains one of the most popular and powerful chemical engineering programs used both industrially and academically.

Teach Yourself the Basics of Aspen Plus, Second Edition continues to deliver important fundamentals on using Aspen Plus software. The new edition focuses on the newest version of Aspen Plus and covers the newest functionalities. Lecture-style chapters set the tone for maximizing the learning experience by presenting material in a manner that emulates an actual workshop classroom environment. Important points are emphasized through encouragement of hands-on learning techniques that direct learners toward achievement in creating effective designs fluidly and with confidence. Teach Yourself the Basics of Aspen Plus, Second Edition includes:





Examples embedded within the text to focus the reader on specific aspects of the material being covered Workshops at the end of each chapter that provide opportunities to test the reader's knowledge in that chapter's subject matter Functionalities covered in the newest version of Aspen including the solution of a flowsheet by an equation oriented, EO approach, and the solution of problems which involve electrolyte equilibria Aspen Plus executable format as well as .txt format files containing details of the examples and the workshops as well as their solutions are provided as a download

Designed with both students and professionals in mind, Teach Yourself the Basics of Aspen Plus, Second Edition is like having a personal professor 24/7. Its revolutionary format is an exciting way to learn how to operate this highly sophisticated softwareand a surefire way for readers to get the results they expect.
Preface to the Second Edition xiii
Preface to the First Edition xv
Acknowledgments xix
About the Companion Website xxi
1 Introduction to Aspen Plus
1(20)
1.1 Basic Ideas
1(3)
1.2 Starting Aspen Plus
4(2)
1.3 The Next Function
6(1)
1.4 The Navigation Pane
6(2)
1.5 The Property Environment
8(3)
1.6 Properties for Simulation
11(2)
1.7 The Simulation Environment
13(1)
1.8 Simulation Options
13(1)
1.9 Units
14(1)
1.10 Streams
15(1)
1.11 Blocks
16(1)
1.12 The Object Manager
17(1)
1.13 Model Execution
17(1)
1.14 Viewing Results
18(2)
1.15 Plotting Results
20(1)
References
20(1)
2 Properties
21(14)
2.1 Introduction
21(1)
2.2 The Pure Component Databanks
22(3)
2.3 Property Analysis
25(4)
2.4 Property Estimation
29(3)
2.5 Workshops
32(1)
2.6 Workshop Notes
33(2)
References
34(1)
3 The Simple Blocks
35(12)
3.1 Introduction
35(1)
3.2 Mixer/Splitter Blocks
35(2)
3.2.1 The Mixer Block
36(1)
3.2.2 The Fsplit Block
36(1)
3.3 The Simple Separator Blocks
37(3)
3.3.1 The Sep Block
38(1)
3.3.2 The Sep2 Block
39(1)
3.4 Some Manipulator Blocks
40(3)
3.4.1 The Dupl Block
40(2)
3.4.2 The Mult Block
42(1)
3.5 Workshops
43(1)
3.6 Workshop Notes
44(3)
4 Processes with Recycle
47(10)
4.1 Introduction
47(1)
4.2 Blocks with Recycle
48(3)
4.3 Heuristics
51(1)
4.4 Workshops
51(4)
4.5 Workshop Notes
55(2)
References
56(1)
5 Flowsheeting and Model Analysis Tools
57(16)
5.1 Introduction
57(1)
5.2 Introduction to Fortran in Aspen Plus
58(1)
5.3 Basic Interpreted Fortran Capabilities
58(3)
5.3.1 Primary Fortran Operators
59(1)
5.3.2 Precedence of Calculations
59(1)
5.3.3 Statement Format
60(1)
5.3.4 Program Logic Control
60(1)
5.4 The Sensitivity Function
61(2)
5.5 The Design Specification
63(2)
5.6 The Calculator Function
65(3)
5.7 The Transfer Function
68(1)
5.8 Workshops
69(2)
5.9 Workshop Notes
71(2)
References
71(2)
6 The Data Regression System (DRS)
73(26)
6.1 Introduction
73(1)
6.2 Parameters of Equations of State
74(2)
6.3 Parameters of Activity Coefficient Equations
76(2)
6.4 Basic Ideas of Regression
78(2)
6.5 The Mathematics of Regression
80(2)
6.5.1 Newton--Raphson Method for Solution of Nonlinear Equations
80(2)
6.5.2 Direct Optimization of an Objective Function
82(1)
6.6 Practical Aspects of Regression of VLE or LLE Data
82(8)
6.6.1 Regression of VLE Data
83(3)
6.6.2 Regression of LLE Data
86(4)
6.7 VLE and LLE Data Sources
90(3)
6.8 Workshops
93(2)
6.9 Workshop Notes
95(4)
References
96(3)
7 Flashes and Decanter
99(12)
7.1 Introduction
99(1)
7.2 The Flash2 Block
99(5)
7.3 The Flash3 Block
104(1)
7.4 The Decanter Block
105(2)
7.5 Workshops
107(1)
7.6 Workshop Notes
108(3)
References
109(2)
8 Pressure Changers
111(6)
8.1 Introduction
111(1)
8.2 The Pump Block
111(1)
8.3 The Compr Block
112(1)
8.4 The MCompr Block
113(1)
8.5 Pipelines and Fittings
114(1)
8.6 Workshops
115(1)
8.7 Workshop Notes
116(1)
References
116(1)
9 Heat Exchangers
117(14)
9.1 Introduction
117(1)
9.2 The Heater Block
118(4)
9.3 The Heatx Block
122(4)
9.4 The Mheatx Block
126(1)
9.5 Workshops
127(1)
9.6 Workshop Notes
128(3)
References
129(2)
10 Reactors
131(22)
10.1 Introduction
131(1)
10.2 The RStoic Block
132(1)
10.3 The RYield Block
133(2)
10.4 The REquil Block
135(1)
10.5 The RGibbs Block
136(2)
10.6 Reactions for the Rigorous Models
138(5)
10.6.1 The Equilibrium Class
139(1)
10.6.2 The Powerlaw Class
139(2)
10.6.3 The Langmuir--Hinshelwood--Hougen--Watson (LHHW) Class
141(1)
10.6.4 The Generalized Langmuir--Hinshelwood--Hougen--Watson Class (GLHHW)
142(1)
10.7 The RCSTR Block
143(1)
10.8 The RPlug Block
143(2)
10.9 The RBatch Block
145(3)
10.10 Workshops
148(2)
10.11 Workshop Notes
150(3)
References
151(2)
11 Multistage Equilibrium Separators
153(30)
11.1 Introduction
153(1)
11.2 The Basic Equations
153(3)
11.3 The Design Problem
156(4)
11.4 A Three-Product Distillation Example
160(2)
11.5 Preliminary Design and Rating Models
162(3)
11.5.1 DSTWU
162(3)
11.5.2 Distl
165(1)
11.6 Rigorous Models
165(9)
11.6.1 RadFrac
168(5)
11.6.2 Extract
173(1)
11.7 BatchSep
174(4)
11.8 Workshops
178(1)
11.9 Workshop Notes
179(4)
References
181(2)
12 Process Flowsheet Development
183(14)
12.1 Introduction
183(1)
12.2 Heuristics
184(1)
12.3 An Example -- The Production of Styrene
184(1)
12.4 A Model with Basic Blocks
185(1)
12.5 Properties
185(2)
12.6 Rigorous Flash and Decanter
187(1)
12.7 Analyzing the Rigorous Distillation
188(1)
12.8 Integrating the Rigorous Distillation into the Flowsheet
189(3)
12.8.1 Selection of the Tear Stream
191(1)
12.8.2 Sequence of Calculations
191(1)
12.9 The Reactor Feed
192(1)
12.10 Miscellaneous Considerations
192(1)
12.11 Workshops
192(3)
12.12 Workshop Notes
195(2)
Reference
196(1)
13 Optimization
197(10)
13.1 Introduction
197(1)
13.2 An Optimization Example
198(4)
13.3 Workshops
202(1)
13.4 Workshop Notes
203(4)
References
205(2)
14 Complex Equilibrium Stage Separations
207(14)
14.1 Introduction
207(1)
14.2 Energy Integration Applications
208(2)
14.3 Homogeneous Azeotropic Distillation
210(1)
14.4 Extractive Distillation
211(3)
14.5 Heterogeneous Operations
214(1)
14.6 Workshops
215(2)
14.7 Workshop Notes
217(4)
References
219(2)
15 Equation-Oriented Simulation
221(22)
15.1 Introduction
221(1)
15.2 Identification of Variables
222(1)
15.3 Equations for EO Simulation
223(2)
15.4 Solving the EO Equations
225(2)
15.5 Comparing Calculated Variables in SM and EO Simulation
227(1)
15.6 Synchronization of the Equations
228(1)
15.7 The Equation Oriented Menu
229(1)
15.8 Solution of an EO Problem
230(2)
15.9 Reinitialization
232(1)
15.10 A Design Specification
233(1)
15.11 An SM Problem That is Difficult to Converge
234(1)
15.12 Sensitivity Analysis
235(1)
15.13 Equation-Oriented Optimization
235(3)
15.14 Workshops
238(3)
15.15 Workshop Notes
241(2)
References
241(2)
16 Electrolytes
243(8)
16.1 Introduction
243(1)
16.2 Electrolyte Solution Equilibria
243(1)
16.3 Electrolyte Solution Equilibria and the Electrolyte Wizard
244(4)
16.4 Electrolyte Equilibrium/Phase Equilibrium Examples
248(3)
16.4.1 Concentration of an Hydrochloric Acid--Water Solution
248(2)
16.4.2 Steam Stripping of Solvents in an Aspen Plus Example
250(1)
References
250(1)
17 Beyond the Basics of Aspen Plus
251(2)
Index 253
Ralph Schefflan has been an adjunct professor at Stevens Institute of Technology for the past thirty-five years. He has taught four graduate courses, thermodynamics, process simulation, numerical methods, and equilibrium stage operations during his time there as well as being SIT's representative to Aspen Technology. Dr. Schefflan introduced process simulation at SIT evolving from Flowtran to Aspen Plus and taught it for thirty years.