Upgrading Oilsands Bitumen and Heavy Oil
-
ParMurray R. Gray (Auteur)
Livre numérique
0 Avis(s), critique(s) et commentaire(s)
"The emphasis throughout is to link the fundamentals of the molecules through to the economic drivers for the industry, because this combination determines the technology used for processing."-From the Introduction The high demand for quality petroleum products necessitates ongoing innovation in the science and engineering underlying oilsands extraction and upgrading. Beginning with a thorough grounding in the composition, fluid properties, reaction behaviour, and economics of bitumen and heavy oil, Murray Gray then delves into current processing technologies, particularly those used at full commercial scale. The tables of data on composition, yield, and behaviour of oilsands bitumen and heavy oil fractions are extensive. Though the focus is on bitumen from Alberta's oilsands-the largest resource in the world-the science applies to upgrading of heavy oil and petroleum residue feeds worldwide. Upgrading Oilsands Bitumen and Heavy Oil lays out the current best practice for engineers and scientists in the oilsands and refining industries, government personnel, academics, and students.
Table des matières
| Front cover | 1 |
|---|---|
| Title page | 4 |
| Copyright page | 5 |
| Dedication | 6 |
| Contents | 8 |
| Acknowledgements | 12 |
| Introduction | 14 |
| I.1 Crude Oil and Bitumen Definitions | 15 |
| I.2 Canadian Oilsands Resources | 15 |
| I.3 International Bitumen and Heavy Oil Reserves | 18 |
| I.4 Upgrading Bitumen and Heavy Oil | 19 |
| I.5 Economic Incentives for Upgrading | 20 |
| I.6 Outline of This Book | 23 |
| References | 24 |
| 1 Density and Phase Behaviour | 26 |
| 1.1 Density and API Gravity | 28 |
| 1.2 Distillation Curves and Boiling Ranges | 30 |
| 1.3 Average Molar Mass and Molar Mass Distribution | 37 |
| 1.4 Vapour–Liquid Equilibrium | 43 |
| 1.5 Solids in Crude and Processed Oils | 54 |
| 1.6 Density and Average Molar Mass of Asphaltenes | 59 |
| 1.7 Solubility Parameters of the Petroleum, Bitumen and Asphaltene Fractions | 60 |
| 1.8 Water in Hydrocarbons | 74 |
| Abbreviations | 78 |
| Notation | 78 |
| References | 80 |
| 2 Transport and Thermal Properties | 84 |
| 2.1 Liquid Viscosity | 85 |
| 2.2 Thermal Conductivity | 91 |
| 2.3 Diffusion Coefficient | 92 |
| 2.4 Surface Tension | 93 |
| 2.5 Melting Point of Vacuum Residues and Asphaltenes | 95 |
| 2.6 Thermal Properties of Bitumen Fractions | 97 |
| 2.7 Heats of Combustion | 100 |
| Notation | 100 |
| References | 102 |
| 3 Chemical Composition | 104 |
| 3.1 Origins of Alberta Bitumens | 106 |
| 3.2 Elemental Composition | 106 |
| 3.3 Class Fractionation | 112 |
| 3.4 Coke-Forming Tendency | 117 |
| 3.5 Chemical Structures in Bitumen | 120 |
| 3.6 Asphaltene Composition and Structure | 134 |
| 3.7 Quality Issues with Bitumen, Heavy Oils and Oilsands Products | 152 |
| Abbreviations | 155 |
| References | 155 |
| 4 Upgrading Reactions and Kinetics | 162 |
| 4.1 Thermodynamics of Cracking | 164 |
| 4.2 Mechanisms of Cracking Hydrocarbons | 166 |
| 4.3 Overall Kinetics of Bitumen Cracking | 184 |
| 4.4 Liquid- versus Vapour-Phase Cracking of Bitumen Components | 191 |
| 4.5 Catalytic Reactions in Upgrading | 193 |
| 4.6 Formation of Solids and Coke | 203 |
| 4.7 Basic Equations for Reactor Analysis at Steady State | 212 |
| Abbreviations | 215 |
| Notation | 215 |
| References | 217 |
| 5 Marketing of Bitumen Products | 222 |
| 5.1 Crude Oil Exports | 223 |
| 5.2 Crude Oil Pricing | 224 |
| 5.3 Transportation of Bitumen and Upgraded Products | 228 |
| 5.4 Trade-Offs Between Upgrading Cost and Product Quality | 234 |
| 5.5 Natural Gas Supply and Properties | 237 |
| 5.6 Natural Gas Condensate | 241 |
| 5.7 Sulfur Transport and Marketing | 241 |
| References | 242 |
| 6 Production of Bitumen and Heavy Oil | 244 |
| 6.1 Mineable Oilsands | 245 |
| 6.2 In Situ Production of Oilsands Bitumen | 251 |
| 6.3 Improvements to In Situ Production | 254 |
| 6.4 In Situ Upgrading Schemes | 255 |
| References | 258 |
| 7 Overview of Upgrading Processing and Economics | 260 |
| 7.1 Sequences of Upgrading Processes | 261 |
| 7.2 Operating Costs of Upgrading Bitumen and Heavy Oil | 269 |
| 7.3 Benchmarking of Production and Upgrading Strategies | 272 |
| 7.4 Greenhouse Gas Emissions from Production and Upgrading Processes | 275 |
| 7.5 Selection of a Primary Upgrading Technology | 276 |
| 7.6 Relationships of Upgrading to Refining | 279 |
| 7.7 Limits to Upgrading Heavy Oils and Bitumens | 283 |
| References | 285 |
| 8 Separation Processes | 288 |
| 8.1 Desalting | 289 |
| 8.2 Atmospheric and Vacuum Distillation | 295 |
| 8.3 Solvent Deasphalting | 296 |
| References | 307 |
| 9 Thermal Cracking and Coking Processes | 308 |
| 9.1 Visbreaking: Thermal Viscosity Reduction | 309 |
| 9.2 Delayed Coking | 318 |
| 9.3 Fluid Coking | 325 |
| 9.4 Fluid Coking with Coke Gasification | 328 |
| 9.5 Limits on Yield and Density for Coking and Thermal Cracking Products | 329 |
| 9.6 Coke Yield and Composition | 332 |
| 9.7 Recycle in Coking Processes | 335 |
| 9.8 Liquid-Phase Mass Transfer in Coking Processes | 339 |
| 9.9 Additives to Control Coke Yield | 342 |
| 9.10 Development of New Coking Processes | 343 |
| 9.11 Control of Sulfur Emissions from Coking Processes | 349 |
| 9.12 Kinetic Modelling of Thermal Cracking and Coking Processes | 349 |
| 9.13 Heat of Reaction of Visbreaking and Coking | 357 |
| Notation | 358 |
| References | 359 |
| 10 Residue Hydroconversion Processes | 364 |
| 10.1 Fixed-Bed Catalytic Processes | 366 |
| 10.2 Catalytic Ebullated-Bed Processes: LC-Fining and H-Oil | 369 |
| 10.3 Additive-Based Processes: Slurries, Suspensions and Solutions | 380 |
| 10.4 Roles of Hydrogen and Catalysts in Suppressing Coke Formation | 387 |
| 10.5 Limits to the Performance of HydroconversionProcesses | 390 |
| 10.6 Hydrogenation Reactions During Hydroconversion | 392 |
| 10.7 Heat of Reaction for Hydroconversion | 397 |
| 10.8 Catalyst Deactivation in Hydroconversion | 398 |
| 10.9 Kinetic Models of Hydroconversion | 410 |
| Notation | 414 |
| References | 415 |
| 11 Hydrotreating Processes | 418 |
| 11.1 Hydrotreating of Distillate Fractions | 419 |
| 11.2 Conversion of Diolefins | 424 |
| 11.3 Hydrotreating for Aromatics Saturation | 425 |
| 11.4 Hydrocracking of Gas Oils | 429 |
| 11.5 Hydrogenation Reactions During Hydrotreating | 430 |
| 11.6 Stoichiometry of Catalytic Hydrogenation | 437 |
| 11.7 Heats of Reaction of Hydrotreating Reactions | 438 |
| 11.8 Catalyst Properties | 438 |
| 11.9 Catalyst Deactivation | 443 |
| Notation | 450 |
| References | 451 |
| 12 Hydrogen Production and Gas Purification Processes | 454 |
| 12.1 Hydrogen Production Processes | 455 |
| 12.2 Cost of Hydrogen Production | 460 |
| 12.3 Purification of Hydrogen-Rich Process Streams | 461 |
| 12.4 Gas Recovery | 462 |
| 12.5 Amine Treating | 463 |
| 12.6 Sulfur Removal | 465 |
| References | 470 |
| Appendix A Glossary and List of Acronyms | 472 |
| A.1 Glossary of Selected Terms Commonly Used in theOilsands Industry | 472 |
| A.2 Common Acronyms in the Oilsands Industry | 483 |
| References | 483 |
| Appendix B Assay Data for Bitumen and Upgraded Products | 484 |
| Index | 492 |
| About the Author | 513 |
Accessibilité
Aucune donnée d'accessibilité n'est disponible pour cette publication.
Biographies des auteurs
À propos de Murray R. Gray
Murray R. Gray was the founding Director of the Institute for Oil Sands Innovation at the University of Alberta in Edmonton. His research as a professor of chemical engineering specialized in processing of oil sands bitumen and heavy oil.
Avis et commentaires
Compléments
Détails du livre
- Éditeur
- Pica Pica Press
- Catégories
- Chimie industrielle et génie chimique, Énergie, Géologie, géomorphologie et lithosphère, Technologie des combustibles fossiles
- Parution
- Avril 2015
- Pages
- 496
- Chapitres
- 141
- Langue
- Anglais
- ISBN Papier
- 9781772120356
- ISBN PDF
- 9781772120226