Buch, Englisch, 272 Seiten, Format (B × H): 155 mm x 231 mm, Gewicht: 2776 g
Buch, Englisch, 272 Seiten, Format (B × H): 155 mm x 231 mm, Gewicht: 2776 g
ISBN: 978-1-118-93866-9
Verlag: Wiley
Written by some of the most well-known and respected chemical and process engineers working with natural gas today, the chapters in this important volume represent the most cutting-edge and state-of-the-art processes and operations being used in the field. Not available anywhere else, this volume is a must-have for any chemical engineer, chemist, or process engineer working with natural gas.
There are updates of new technologies in other related areas of natural gas, in addition to the CO2 capture and acid gas injection, including testing, reservoir simulations, and natural gas hydrate formations. Advances in Natural Gas Engineering is an ongoing series of books meant to form the basis for the working library of any engineer working in natural gas today. Every volume is a must-have for any engineer or library.
Autoren/Hrsg.
Weitere Infos & Material
Preface xiii
1 Enthalpies of Carbon Dioxide-Methane and Carbon Dioxide-Nitrogen Mixtures: Comparison with Thermodynamic Models 1
Erin L. Roberts and John J. Carroll
1.1 Introduction 1
1.2 Enthalpy 2
1.3 Literature Review 2
1.3.1 Carbon Dioxide-Methane 4
1.3.2 Carbon Dioxide-Nitrogen 4
1.4 Calculations 5
1.4.1 Benedict-Webb-Rubin 6
1.4.2 Lee-Kesler 12
1.4.3 Soave-Redlich-Kwong 17
1.4.4 Peng-Robinson 23
1.4.5 AQUAlibrium 28
1.5 Discussion 33
1.6 Conclusion 36
References 37
2 Enthalpies of Hydrogen Sulfide-Methane Mixture: Comparison with Thermodynamic Models 39
Erin L. Roberts and John J. Carroll
2.1 Introduction 39
2.2 Enthalpy 40
2.3 Literature Review 40
2.4 Calculations 41
2.4.1 Lee-Kesler 41
2.4.2 Benedict-Webb-Rubin 43
2.4.3 Soave-Redlich-Kwong 43
2.4.4 Redlich-Kwong 47
2.4.5 Peng-Robinson 47
2.4.6 AQUAlibrium 50
2.5 Discussion 50
2.6 Conclusion 52
References 54
3 Phase Behavior and Reaction Thermodynamics Involving Dense-Phase CO2 Impurities 55
J.A. Commodore, C.E. Deering and R.A. Marriott
3.1 Introduction 55
3.2 Experimental 57
3.3 Results and Discussion 58
3.3.1 Phase Behavior Studies of SO2 Dissolved in Dense CO2 Fluid 58
3.3.2 The Densimetric Properties of CS2 and CO2 Mixtures 60
References 61
4 Sulfur Recovery in High Density CO2 Fluid 63
S. Lee and R.A. Marriott
4.1 Introduction 64
4.2 Literature Review 64
4.3 Methodology 65
4.4 Results and Discussion 66
4.5 Conclusion and Future Directions 67
References 68
5 Carbon Capture Performance of Seven Novel Immidazolium and Pyridinium Based Ionic Liquids 71
Mohamed Zoubeik, Mohanned Mohamedali and Amr Henni
5.1 Introduction 71
5.2 Experimental Work 73
5.2.1 Materials 73
5.2.2 Density Measurement 73
5.2.3 Solubility Measurement 73
5.3 Modeling 76
5.3.1 Calculation of Henry’s Law Constants 76
5.3.2 Critical Properties Calculations 76
5.3.3 Peng Robinson EoS 76
5.4 Results and Discussion 77
5.4.1 Density 77
5.4.2 Critical Properties 77
5.4.3 CO2 Solubility 78
5.4.4 The Effect of Changing the Cation 81
5.4.5 The Effect of Changing the Anion 84
5.4.6 Henry’s Law Constant, Enthalpy and Entropy Calculations 85
5.4.7 Thermodynamic Modeling of CO2 Solubility 86
5.5 Conclusion 87
Acknowledgements 88
References 88
6 Vitrisol a 100% Selective Process for H2S Removal in the Presence of CO2 91
W.N. Wermink, N. Ramachandran, and G.F. Versteeg
6.1 Introduction 92
6.2 Case Definition 94
6.3 “Amine-Treated” Cases by PPS 95
6.3.1 Introduction to PPS 95
6.3.2 Process Description 96
6.3.3 PFD 97
6.3.4 Results 97
6.3.4.1 Case 1 97
6.3.4.2 Case 2 97
6.4 VitrisolƒòƒnProcess Extended with Regeneration of Active Component 99
6.4.1 Technology Description 99
6.4.2 Parameters Determining the Process Boundary Conditions 99
6.4.3 Absorption Section 101
6.4.4 Regeneration Section 102
6.4.5 Sulphur Recovery Section 104
6.4.6 CO2-Absorber 105
6.4.7 PFD 105
6.5 Results 105
6.6 Discussion 110
6.6.1 Comparison of Amine Treating Solutions to Vitrisolƒòƒn110
6.6.2 Enhanced H2S Removal of Barnett Shale Gas (case 2) 112viii Contents
6.7 Conclusions 113
6.8 Notation 115
References 115
Appendix 6-A: H&M Balance of Case 1 (British Columbia shale) of the Amine Process 117
Appendix 6-B H&M Balance of Case 2a (Barnett shale) of the Amine Process with Stripper Promoter 119
Appendix 6-C H&M Balance of Case 3 (Barnett shale) of the Amine Process (MEA) 121
Appendix 6-D: H&M Balance of C