Search citation statements
Paper Sections
Citation Types
Year Published
Publication Types
Relationship
Authors
Journals
This is final report for contract DE-AC26-99BC15211. The report describes progress made in the various thrust areas of the project, which include internal drives for oil recovery, vapor-liquid flows, comb ustion and reaction processes and the flow of fluids with yield stress. The report consists mainly of a compilation of various topical reports, technical papers and research reports published produced during the three-year project, which ended on May 6, 2002 and was no-cost extended to January 5, 2003. Advances in multiple processes and at various scales are described.In the area of internal drives, significant research accomplishments were made in the modeling of gas-phase growth driven by mass transfer, as in solution-gas drive, and by heat transfer, as in internal steam drives. In the area of vapor-liquid flows, we studied various aspects of concurrent and countercurrent flows, including stability analyses of vapor-liquid counterflow, and the development of novel methods for the pore-network modeling of the mobilization of trapped phases and liquid-vapor phase changes. In the area of combustion, we developed new methods for the modeling of these processes at the continuum and pore-network scales. These models allow us to understand a number of important aspects of in-situ combustion, including steady-state front propagation, multiple steady-states, effects of heterogeneity and modes of combustion (forward or reverse). Additional aspects of reactive transport in porous media were also studied.Finally, significant advances were made in the flow and displacement of non-Newtonian fluids with Bingham plastic rheology, which is characteristic of various heavy oil processes. Various accomplishments in generic displacements in porous media and corresponding effects of reservoir heterogeneity are also cited.A total of 44 publications in refereed journals and/or in scientific conferences resulted from this project. In addition, several papers are under preparation at the time of the writing of this report. The support provided by the contract also allowed the completion of 6 PhD Theses, with two more under way. This research output would have been impossible without this support, for which the PI and the students are grateful. vii EXECUTIVE SUMMARYThis is the final report of an investigation on the various multi-phase and multiscale transport and reaction processes associated with heavy oil recovery. As we reported in detail in three previous annual reports, the thrust areas in this study include the following:Internal drives, vapor-liquid flows, combustion and reaction processes, fluid displacements, the effect of instabilities and heterogeneities, and the flow of fluids with yield stress. These find respective applications to: foamy oils, the evolution of dissolved gas, internal steam drives, the mechanics of concurrent and countercurrent vapor-liquid flows, associated with thermal methods and steam injection, such as SAGD, the in-situ combustion, the upscaling of displacements in heterogeneous media, the fl...
This is final report for contract DE-AC26-99BC15211. The report describes progress made in the various thrust areas of the project, which include internal drives for oil recovery, vapor-liquid flows, comb ustion and reaction processes and the flow of fluids with yield stress. The report consists mainly of a compilation of various topical reports, technical papers and research reports published produced during the three-year project, which ended on May 6, 2002 and was no-cost extended to January 5, 2003. Advances in multiple processes and at various scales are described.In the area of internal drives, significant research accomplishments were made in the modeling of gas-phase growth driven by mass transfer, as in solution-gas drive, and by heat transfer, as in internal steam drives. In the area of vapor-liquid flows, we studied various aspects of concurrent and countercurrent flows, including stability analyses of vapor-liquid counterflow, and the development of novel methods for the pore-network modeling of the mobilization of trapped phases and liquid-vapor phase changes. In the area of combustion, we developed new methods for the modeling of these processes at the continuum and pore-network scales. These models allow us to understand a number of important aspects of in-situ combustion, including steady-state front propagation, multiple steady-states, effects of heterogeneity and modes of combustion (forward or reverse). Additional aspects of reactive transport in porous media were also studied.Finally, significant advances were made in the flow and displacement of non-Newtonian fluids with Bingham plastic rheology, which is characteristic of various heavy oil processes. Various accomplishments in generic displacements in porous media and corresponding effects of reservoir heterogeneity are also cited.A total of 44 publications in refereed journals and/or in scientific conferences resulted from this project. In addition, several papers are under preparation at the time of the writing of this report. The support provided by the contract also allowed the completion of 6 PhD Theses, with two more under way. This research output would have been impossible without this support, for which the PI and the students are grateful. vii EXECUTIVE SUMMARYThis is the final report of an investigation on the various multi-phase and multiscale transport and reaction processes associated with heavy oil recovery. As we reported in detail in three previous annual reports, the thrust areas in this study include the following:Internal drives, vapor-liquid flows, combustion and reaction processes, fluid displacements, the effect of instabilities and heterogeneities, and the flow of fluids with yield stress. These find respective applications to: foamy oils, the evolution of dissolved gas, internal steam drives, the mechanics of concurrent and countercurrent vapor-liquid flows, associated with thermal methods and steam injection, such as SAGD, the in-situ combustion, the upscaling of displacements in heterogeneous media, the fl...
Abstract:In this work, internal moisture profiles obtained either by simulation or experimentally during the convective drying of resorcinol-formaldehyde gels are compared. Such a comparison constitutes an attractive way to validate drying simulation models. X-ray microtomography, a powerful 3D imaging technique, coupled to image analysis is used to determine the internal moisture profiles in a non destructive way. A thermo-hygro-mechanical coupled model is used to simulate the moisture profiles developing during drying. Resorcinol-formaldehyde gels are used because their degree of shrinkage can be easily controlled. Results show a fairly good agreement between experimental and simulated profiles, especially at high moisture contents.
The article contains sections titled: 1. Introduction 1.1. Definition and History 1.2. The Development of Adsorption Technology 1.3. Adsorbents and Processes for Separation of Gases and Liquids 2. Adsorption Apparatus 2.1. Gas Phase Adsorption 2.2. Liquid‐Phase Adsorption 3. Adsorbents 3.1. Oxidic Hydrophilic Adsorbents 3.2. Carbon‐Containing Adsorbents 3.3. Chemical Complexing Sorbents 4. Thermodynamics, Equilibria, and Heat of Adsorption 4.1. Explicit Equilibria 4.1.1. Single‐Component Pure‐Gas Equilibria 4.1.2. Temperature Dependence of the Saturation Loading 4.2. Adsorption Enthalpy 4.2.1. Differential Adsorption Enthalpies 4.2.2. Integral Adsorption Enthalpies 4.3. Mixture Equilibria 4.3.1. Homogeneous Surfaces 4.3.2. Mixture BET Equation 4.3.3. Ideal Adsorbed Solution Theory 4.3.3.1. Spreading Pressure 4.3.3.2. Examples for Binary Mixture Calculations 4.3.3.2.1. Given Gas‐Phase Concentration 4.3.3.2.2. Given Loading 4.3.4. Statistical Thermodynamics Model 5. Kinetics 5.1. External/Internal Transport 5.1.1. Internal Resistances 5.1.2. Linear Driving Force and Other Models 6. Adsorber Dynamics 6.1. Modeling the Isothermal Fixed‐Bed Adsorber 6.2. Modeling the Adiabatic Fixed‐Bed Adsorber 6.2.1. Loading and Breakthrough Curves 6.2.2. Simplified Models 6.2.3. Coefficients 7. Regeneration of Adsorbents 7.1. Regeneration by Temperature Swing 7.2. Regeneration by Pressure Swing 7.3. Regeneration by Displacement 7.4. Regeneration by Extraction 7.5. Reactivation of Adsorbents 7.6. Liquid Phase Desorption 8. Gas Phase Processes 8.1. Adsorptive Separation of Gas Mixtures 8.2. Pressure Swing Processes 8.3. Separation of Nitrogen from Oxygen 8.4. Adsorptive Purification of Air 8.5. Removal of Radioactive Nuclides from Exhaust Gas 8.6. Removal of Organic Components from Exhaust Air 8.7. Adsorptive Desulfurization Processes 8.8. Adsorptive Purification of Methane 8.9. Adsorptive Purification of Hydrogen 8.10. Separation of Isomers 9. Liquid‐Phase Processes 9.1. Purification of Drinking Water 9.2. Wastewater Treatment 9.3. Separation of Nonaqueous Substances
scite is a Brooklyn-based organization that helps researchers better discover and understand research articles through Smart Citations–citations that display the context of the citation and describe whether the article provides supporting or contrasting evidence. scite is used by students and researchers from around the world and is funded in part by the National Science Foundation and the National Institute on Drug Abuse of the National Institutes of Health.
hi@scite.ai
10624 S. Eastern Ave., Ste. A-614
Henderson, NV 89052, USA
Copyright © 2024 scite LLC. All rights reserved.
Made with 💙 for researchers
Part of the Research Solutions Family.