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Vapor-liquid equilibria using UNIFAC : a group contribution method /
Vapor-Liquid Equilibria Using Unifac.
| Clasificación: | Libro Electrónico |
|---|---|
| Autores principales: | , , |
| Formato: | Electrónico eBook |
| Idioma: | Inglés |
| Publicado: |
Amsterdam ; New York : New York :
Elsevier Scientific Pub. Co. ; Distributors for the U.S. and Canada, Elsevier North-Holland,
1977, 1979 printing.
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| Temas: | |
| Acceso en línea: | Texto completo |
MARC
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| 100 | 1 | |a Fredenslund, Aage, |d 1941- | |
| 245 | 1 | 0 | |a Vapor-liquid equilibria using UNIFAC : |b a group contribution method / |c Aage Fredenslund, J�urgen Gmehling and Peter Rasmussen. |
| 260 | |a Amsterdam ; |a New York : |b Elsevier Scientific Pub. Co. ; |a New York : |b Distributors for the U.S. and Canada, Elsevier North-Holland, |c 1977, 1979 printing. | ||
| 300 | |a 1 online resource (xi, 380 pages) : |b illustrations | ||
| 336 | |a text |b txt |2 rdacontent | ||
| 337 | |a computer |b c |2 rdamedia | ||
| 338 | |a online resource |b cr |2 rdacarrier | ||
| 504 | |a Includes bibliographical references. | ||
| 506 | |3 Use copy |f Restrictions unspecified |2 star |5 MiAaHDL | ||
| 533 | |a Electronic reproduction. |b [Place of publication not identified] : |c HathiTrust Digital Library, |d 2010. |5 MiAaHDL | ||
| 538 | |a Master and use copy. Digital master created according to Benchmark for Faithful Digital Reproductions of Monographs and Serials, Version 1. Digital Library Federation, December 2002. |u http://purl.oclc.org/DLF/benchrepro0212 |5 MiAaHDL | ||
| 583 | 1 | |a digitized |c 2010 |h HathiTrust Digital Library |l committed to preserve |2 pda |5 MiAaHDL | |
| 588 | 0 | |a Print version record. | |
| 505 | 0 | |a Front Cover; Vapor-Liquid Equilibria Using UNIFAC; Copyright Page; PREFACE; Table of Contents; CHAPTER 1. INTRODUCTION; 1.1 The Phase Equilibrium Problem; 1.2 Origin and Range of Applicability of The Unifac Method; 1.3 Oraanization of The Book; CHAPTER 2. VAPOR PHASE NONIDEALITY; 2.1 Fugacity Coefficients From The Virial Equation; 2.2 Second Virial Coefficients; 2.3 Fugacity Coefficients From The Chemical Theory; 2.4 Computer Program For Fugacity Coefficients; CHAPTER 3. LIQUID PHASE NONIDEALITY; 3.1 Calculation of Reference Fugacities; 3.2 Activity Coefficients | |
| 505 | 8 | |a CHAPTER 4. THE UNIFAC GROUP-CONTRIBUTION METHOD4.1 The Unifac Model; 4.2 Group Interaction Parameters; 4.3 Sample Predictions; 4.4 Temperature Dependence of The Unifac Parameters; 4.5 Alternative Unifac Parameters For Systems With Alcohols; 4.6 Additional Unifac Parameters; CHAPTER 5. DETERMINATION OF UNIFAC PARAMETERS; 5.1 The Dortmund Data Bank; 5.2 Thermodynamic Consistency; 5.3 Calculation of Activity Coefficients From Mutual Solubility Data; 5.4 Estimation of Unifac Parameters; CHAPTER 6. PREDICTION OF VAPOR-LIQUID EQUILIBRIA IN BINARY SYSTEMS | |
| 505 | 8 | |a 6.1 Sample Results From The Data Correlation6.2 Sample Predictions; 6.3 Predictions For Systems Containing Ethanol; CHAPTER 7. PREDICTION OF VAPOR-LIQUID EQUILIBRIA INMULTICOMPONENT SYSTEMS; CHAPTER 8. PREDICTION OF PHASE-SPLITTING AND EXCESS ENTHALPY; 8.1 Phase-Splitting; 8.2 Excess Enthalpy; CHAPTER 9. APPLICATION OF UNIFAC TO DISTILLATION COLUMN DESIGN; 9.1 Multicomponent Distillation Calculations By Linearization; 9.2 The Column Calculation Procedure; 9.3 Examples of Distillation Calculations (Simplified Version); 9.4 Examples of Distillation Calculations (Full Version) | |
| 505 | 8 | |a APPENDIX 1: CALCULATION OF FUGACITY AND ACTIVITY COEFFICIENTSTHE CONSISTENCY TEST1.1 SVIR; 1.2 PHIB; 1.3 YENWO; 1.4 GAUSL; 1.5 :MLMEN; 1.6 BIJ; 1.7 Thermodynamic Consistency Test; APPENDIX 2: UNIFAC PROGRAMS; UNIFA; SYSTM; GRES; GREF; GCOMB; HCON; Calculation of Activity Coefficients; Prediction of Liquid-Liquid Equilibrium Compositions; Uniquac Parameters From Unifac; APPENDIX 3: ESTIMATION OF UNIFAC PARAMETERS; APPENDIX 4: DISTILLATION PROGRAMS; Main Distillation Program, Full Version; Main distillation program, simplified version | |
| 520 | |a Vapor-Liquid Equilibria Using Unifac. | ||
| 630 | 0 | 0 | |a UNIFAC. |
| 650 | 0 | |a Vapor-liquid equilibrium |x Data processing. | |
| 630 | 0 | 6 | |a UNIFAC (Logiciel) |
| 650 | 6 | |a �Equilibre liquide-vapeur |0 (CaQQLa)201-0042021 |x Informatique. |0 (CaQQLa)201-0380011 | |
| 650 | 7 | |a SCIENCE |x Chemistry |x Industrial & Technical. |2 bisacsh | |
| 650 | 7 | |a TECHNOLOGY & ENGINEERING |x Chemical & Biochemical. |2 bisacsh | |
| 630 | 0 | 7 | |a UNIFAC |2 fast |0 (OCoLC)fst01361545 |
| 650 | 7 | |a Vapor-liquid equilibrium |x Data processing |2 fast |0 (OCoLC)fst01164132 | |
| 650 | 7 | |a Berechnung |2 gnd |0 (DE-588)4120997-7 | |
| 650 | 7 | |a Fl�ussigkeit |2 gnd |0 (DE-588)4017621-6 | |
| 650 | 7 | |a Phasengleichgewicht |2 gnd |0 (DE-588)4132145-5 | |
| 650 | 7 | |a UNIFAC |2 gnd |0 (DE-588)4186893-6 | |
| 650 | 7 | |a Gas |2 gnd |0 (DE-588)4019320-2 | |
| 650 | 1 | 7 | |a Fase-evenwichten. |2 gtt |
| 650 | 1 | 7 | |a Gassen. |2 gtt |
| 650 | 1 | 7 | |a Vloeistoffen. |2 gtt |
| 650 | 1 | 7 | |a Computermethoden. |2 gtt |
| 653 | |a Vapour-liquid equilibria |a Prediction |a Mathematical models | ||
| 700 | 1 | |a Gmehling, J�urgen, |d 1946- |e author. | |
| 700 | 1 | |a Rasmussen, Peter, |d 1935- |e author. | |
| 776 | 0 | 8 | |i Print version: |a Fredenslund, Aage, 1941- |t Vapor-liquid equilibria using UNIFAC. |d Amsterdam ; New York : Elsevier Scientific Pub. Co. ; New York : Distributors for the U.S. and Canada, Elsevier North-Holland, 1977, 1979 printing |w (DLC) 77012218 |w (OCoLC)3240581 |
| 856 | 4 | 0 | |u https://sciencedirect.uam.elogim.com/science/book/9780444416216 |z Texto completo |