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Industrial Chemical Process Design 2nd edition [Kõva köide]

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  • Formaat: Hardback, 432 pages, kõrgus x laius x paksus: 229x211x31 mm, kaal: 957 g, 150 Illustrations
  • Ilmumisaeg: 16-Dec-2013
  • Kirjastus: McGraw-Hill Professional
  • ISBN-10: 0071819800
  • ISBN-13: 9780071819800
Teised raamatud teemal:
Industrial Chemical Process Design 2nd editionSuurem pilt
  • Formaat: Hardback, 432 pages, kõrgus x laius x paksus: 229x211x31 mm, kaal: 957 g, 150 Illustrations
  • Ilmumisaeg: 16-Dec-2013
  • Kirjastus: McGraw-Hill Professional
  • ISBN-10: 0071819800
  • ISBN-13: 9780071819800
Teised raamatud teemal:
Püsilink: https://www.kriso.ee/db/9780071819800.html
Märksõnad:
Process engineer Erwin describes practical process engineering and shows new engineers how to apply what they learned in school to the real world. He covers the database; fractionation and applications of the database; fractionation tray design and rating; oil and gas production surface facility design and rating; shell/tube, plate/frame, and air finfan heat exchangers; fluid flow piping design and rating; the nitrogen oxide air pollution problem and solution; liquid-liquid extraction; and determining the cost of process equipment. Annotation ©2014 Book News, Inc., Portland, OR (booknews.com)

THE MOST COMPLETE AND CURRENT PROBLEM-SOLVING TOOLKIT FOR CHEMICAL ENGINEERS AND PROCESS DESIGNERS

Fully updated for the latest advances in the field, Industrial Chemical Process Design, Second Editionprovides a step-by-step methodology and 25 downloadable, customizable, needs-specific software applicationsthat offer quick, accurate solutions to complex process design problems. These applications uniquely fill the gaps left by large, very expensive commercial process simulation software packages used to select, size, and design industrial chemical process equipment. Written by an expert industry consultant, this revised edition contains new information on:

  • Sustainable energy sources
  • The Fischer Tropsch gas-to-liquids process
  • Ethanol fractionation
  • Mitigation solutions for atmospheric pollutants, including nitrogen oxides (NOx)
  • And more

Featuring more than 200 illustrations, this practical, comprehensive resource presents complex operations and formulas in an easy-to-understand way and demonstrates how to incorporate helpful software tools into your daily practice.

Coverage includes:

Fractionation tray design and rating * Oil/gas production surface facility design and rating * Shell/tube, air finfan, and plate-frame exchangers * Fluid flow piping design and rating * Liquid-liquid extraction * Process equipment cost determination

Acknowledgments xiii
Introduction: The Quest xv
1 The Database 1(38)
Nomenclature
1(1)
Achieving the Quest
1(6)
Database of Energy Sources
2(1)
Database Biomass (Greenhouse Gases-Petroleum) Energy Conversion
2(2)
Solar Greenhouse Energy
4(1)
The Real Answer to Our Greenhouse Energy Needs
5(1)
Fischer-Tropsch Gas-to-Liquids Process
5(1)
The Sasol FT Slurry Phase Process
6(1)
The Quest
7(1)
Viscosity
7(4)
Liquid Viscosity
7(2)
Gas Viscosity
9(2)
Density
11(6)
Liquid Density
11(6)
Critical Temperature, Tc
17(2)
Critical Pressure, Pc
19(1)
Molecular Weight
20(1)
Boiling Point
21(10)
Crude Oil Characterization-Brief Description of ASTM4
25(5)
ASTM4 Pc Method
30(1)
Acentric Factor
31(1)
ASTM4 Acent Method
31(1)
Enthalpy
31(5)
Mixture Enthalpy Interpolation
35(1)
References
36(3)
2 Fractionation and Applications of the Database 39(28)
Nomenclature
39(2)
Equations of State
41(1)
PPK Accuracy and Limitations
41(1)
The PPK Equation of State
42(1)
Bubble Point
43(6)
Flash Calculations
49(2)
Fractionation: A Shortcut Method
51(10)
Proposed Software Method
51(10)
Overview of Example Problem and Validating
61(1)
Tray-to-Tray Rigorous Program Validation Check
61(2)
Input Specifications
62(1)
Second-Run Input Specifications
62(1)
Ethanol Fractionation Still Shortcut Model
63(1)
Ethanol-Water UniSim Program Simulator Run
63(2)
Hdist Overview
65(1)
References
65(2)
3 Fractionation Tray Design and Rating 67(42)
Nomenclature
67(2)
A Special Note
69(1)
Tray Hydraulics
69(9)
Conventional Tray Design
74(2)
Tray Deck Nonconventional Active Area Design
76(1)
Key Data
77(1)
Tray Design Data
78(14)
General Tray Design Methodology for All Tray Types
78(2)
System Factor
80(1)
Tray Spacing
80(2)
Sloped Downcomers
82(1)
Calculating the Active Area
82(2)
Downcomer Flood Percent Calculation
84(1)
The Importance of Percent Flood Loadings
85(1)
Tray Active Area Calculation
85(1)
Tray VLOAD Factor
85(1)
Nonconventional Tray Active Area Design
86(1)
Tray Efficiency Data
86(2)
Erwin Two-Film Method
88(4)
Valve-Type Tray Design and Rating
92(3)
Valve Tray Capacity Factor
92(1)
Tray Active Area Flood Calculation
93(1)
Valve Tray Pressure Drop Calculation
94(1)
Bubble Cap Tray Design and Rating
95(4)
Bubble Cap Tray Flood Calculation
95(3)
Bubble Cap Pressure Drop Calculation
98(1)
Sieve Tray Design and Rating
99(5)
Sieve Tray Flood
99(3)
Sieve Tray Pressure Drop
102(2)
Tower Random Packing
104(4)
Packing Flood
106(1)
Packing Low-Load Channeling
106(1)
HETP Packing Depth Efficiency
107(1)
Packing Liquid Distribution Trays and Limiting Packing Height
108(1)
References
108(1)
4 Oil and Gas Production Surface Facility Design and Rating 109(38)
Nomenclature
109(1)
A Special Note to the Wise
110(1)
Crude Oil Production Surface Processes
111(1)
First Stabilizer Stage
112(1)
Crude Dehydration
113(5)
Electrostatic Dehydration
114(2)
Free Water
116(1)
Soluble Water
117(1)
Salt Removal
117(1)
Three-Phase Horizontal Separator
118(8)
Vessize Program
118(4)
Gas Phase in Horizontal Separator
122(1)
Oil Phase in Horizontal Separator
123(3)
Three-Phase Vertical Separator
126(1)
Equations
126(1)
Vertical Separators
127(5)
Particle Size
127(5)
Vertical Storage and Treatment Tanks
132(7)
Degasser Vessel
137(1)
Water Knockout Tank
138(1)
Dehydration Tank
138(1)
Methodology for Horizontal Separator Sizing and Rating Calculations
139(2)
Gas Phase
139(1)
Liquid Phase-Separating Water from Oil
140(1)
Production Desalters
141(2)
Equipment Design Basis
141(1)
Methodology
141(2)
The Windows 7 Excel Spreadsheet Software
143(2)
The Greenhouse Applications
144(1)
Overview
145(1)
References
146(1)
5 Shell/Tube, Plate/Frame, and Air Finfan Heat Exchangers 147(50)
Nomenclature
147(3)
Shell/Tube Exchangers
147(1)
Air Finfan Exchangers
148(2)
Shell/Tube Exchanger Practical Design/Rating Equations
150(11)
Tube Side
150(2)
Shell Side
152(2)
Overall Heat Transfer Coefficient
154(1)
Exchanger Fouling Factor Rd
154(1)
Log Mean Temperature Difference
155(1)
Exchanger Rating
155(6)
A General Excel Shell/Tube Heat Exchanger Program Spreadsheet
161(7)
Plate-and-Frame Heat Exchangers
162(1)
Consider the Following Example
163(4)
Using the Charts
167(1)
The Plate-and-Frame Heat Exchanger-An Overview
168(1)
Air Finfan Heat Exchangers
168(20)
Air Finfan Cooler Configurations
169(2)
Air Cooler Sizes
171(2)
Air Finfan Cooler Practical Design
173(2)
Design Methodology
175(13)
Air Finfan Exchanger Computer Programs
188(8)
AirClr8 Applications
188(2)
AirClr9 Applications
190(2)
AirClr8 Program Code Listing
192(1)
Program Summaries
192(4)
Conclusion
196(1)
References
196(1)
6 Fluid Flow Piping Design and Rating 197(42)
Nomenclature
197(1)
Single-Phase Flow
197(1)
Two-Phase Flow
198(1)
Fluid Flow Basics
198(4)
Hydraulic Grade Line
200(1)
Energy Grade Line
200(1)
Bernoulli Equation Terms
200(2)
Single-Phase Flow Equations
202(13)
Friction Factor f
202(2)
Fluid Flow General Equation
204(3)
Valve and Fitting Pressure Losses
207(3)
Conclusions on Single-Phase Flow Equations
210(5)
Two-Phase Flow
215(1)
Introduction
215(1)
The Myth
215(1)
A Solution for All Two-Phase Flow Problems
216(1)
Two-Phase Flow Equations
216(18)
Two-Phase Flow Program TPF
220(1)
Calculation Examples
220(3)
Computer Program Examples
223(11)
Excel Spreadsheet Software
234(4)
Overview
238(1)
References
238(1)
7 The Nitrogen Oxide Air Pollution Problem and Solution 239(14)
Nomenclature
239(1)
The Problem
239(1)
The Solution
240(1)
The SCR Process
241(11)
Calculating Duct Sizing
245(5)
Equations of Figure 7.2
250(2)
An Overview
252(1)
Reference
252(1)
8 Liquid-Liquid Extraction 253(36)
Nomenclature
253(2)
General Definitions
255(1)
Liquid Extraction Equilibria
256(2)
The Rectangular X-Y Equilibrium Diagram
258(12)
Extractor Operation
270(2)
Dispersed Phase
271(1)
General Extraction Operation
272(1)
Equilibrium Stages Overview
273(1)
Choosing the Contactor
273(1)
Stage Efficiency
274(2)
Column Capacity
276(8)
Running the LiqX Program
284(2)
The Greenhouse Applications
286(1)
References
286(3)
9 Process Equipment Cost Determination 289(54)
Nomenclature
289(4)
Installation Cost for Individual Process Items
293(1)
Major Plant Costs
293(39)
Cost Estimation
293(2)
The Fischer-Tropsch Process
295(2)
Summary Form for Cost Estimates
297(35)
Economic Evaluation
332(10)
Definitions
332(10)
References
342(1)
A LMTD Correction Factors 343(20)
B Software Program Exhibits 363(16)
C Raoult's Law 379(18)
Application to Liquid-Liquid Extraction
379(1)
References
380(13)
References of Liquid-Liquid Equilibrium
393(4)
Index 397
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