FRINK Linked Data Fragments server

Matches in SemOpenAlex for { <https://semopenalex.org/work/W2003906068> ?p ?o ?g. }

• W2003906068 abstract "Abstract World production of heavy and extra-heavy oils has increased as the production of conventional crudes decline. However, the conventional oil recovery methods cannot effectively recover the heavy oil due to their high viscosities. The steam and/or solvent-based recovery processes can be considered as an efficient method for recovery of these resources. The performance of these techniques depends on the amount of solvent dissolved in the crude and the variation of oil viscosity with temperature. Thus, full understanding of the quantitative effects of the solvent on heavy oil viscosity and phase behaviours are crucial for feasibility studies, design and prediction of field-scale processes. Phase behaviour study of bitumen diluted with heavy hydrocarbon solvents such as propane and butane have gained less attention in recent years. These solvents, as good candidates for recently developed recovery methods such as Expanding Solvent Steam-Assisted Gravity Drainage (ES-SAGD), would provide promising oil production rates. The aim of this research, thus, is the development of an understanding of the phase behaviour of butane / Athabasca bitumen systems. It deals with both vapor-liquid and liquid-liquid phase equilibriums over wide range of temperatures (up to 200°C) approaching the conditions of in situ steam processes and pressures up to 8 MPa. Experimental results indicated that the vapor-liquid and liquid-liquid equilibrium formed over the studied temperature and pressure ranges. In the case of vapor-liquid equilibrium, the dissolved butane in bitumen leads to a significant oil viscosity reduction. The effect was higher at lower temperature and higher pressure. For liquid-liquid equilibrium, butane extracted light components from oil and formed a butane-enriched phase while the heavier constitutes such as asphaltene separated as second heavy liquid phase. Finally, the measured solubility and density data were adequately modeled with Peng-Robinson equation of state." @default.
• W2003906068 created "2016-06-24" @default.
• W2003906068 creator A5029764196 @default.
• W2003906068 creator A5042005991 @default.
• W2003906068 creator A5058081023 @default.
• W2003906068 date "2014-06-10" @default.
• W2003906068 modified "2023-09-27" @default.
• W2003906068 title "Phase Behaviour Study of Butane / Athabasca Bitumen Mixtures Applicable for Thermal and Hybrid Solvent Recovery Processes" @default.
• W2003906068 cites W1966411484 @default.
• W2003906068 cites W1969174567 @default.
• W2003906068 cites W1975469091 @default.
• W2003906068 cites W1981751659 @default.
• W2003906068 cites W1981906143 @default.
• W2003906068 cites W1984892952 @default.
• W2003906068 cites W1987933112 @default.
• W2003906068 cites W2002569539 @default.
• W2003906068 cites W2002845616 @default.
• W2003906068 cites W2003642111 @default.
• W2003906068 cites W2015958052 @default.
• W2003906068 cites W2019815385 @default.
• W2003906068 cites W2036746235 @default.
• W2003906068 cites W2037485208 @default.
• W2003906068 cites W2053412108 @default.
• W2003906068 cites W2059809197 @default.
• W2003906068 cites W2061161882 @default.
• W2003906068 cites W2069459653 @default.
• W2003906068 cites W2083108397 @default.
• W2003906068 cites W2083237811 @default.
• W2003906068 cites W2086243838 @default.
• W2003906068 cites W2093728273 @default.
• W2003906068 cites W2129288307 @default.
• W2003906068 cites W2133355382 @default.
• W2003906068 cites W2133777675 @default.
• W2003906068 cites W2166603099 @default.
• W2003906068 cites W2315338650 @default.
• W2003906068 cites W2331494623 @default.
• W2003906068 cites W2480945251 @default.
• W2003906068 cites W4229598158 @default.
• W2003906068 cites W1994588165 @default.
• W2003906068 doi "https://doi.org/10.2118/170163-ms" @default.
• W2003906068 hasPublicationYear "2014" @default.
• W2003906068 type Work @default.
• W2003906068 sameAs 2003906068 @default.
• W2003906068 citedByCount "6" @default.
• W2003906068 countsByYear W20039060682016 @default.
• W2003906068 countsByYear W20039060682018 @default.
• W2003906068 countsByYear W20039060682019 @default.
• W2003906068 countsByYear W20039060682023 @default.
• W2003906068 crossrefType "proceedings-article" @default.
• W2003906068 hasAuthorship W2003906068A5029764196 @default.
• W2003906068 hasAuthorship W2003906068A5042005991 @default.
• W2003906068 hasAuthorship W2003906068A5058081023 @default.
• W2003906068 hasConcept C121332964 @default.
• W2003906068 hasConcept C127172972 @default.
• W2003906068 hasConcept C127313418 @default.
• W2003906068 hasConcept C127413603 @default.
• W2003906068 hasConcept C131779963 @default.
• W2003906068 hasConcept C159985019 @default.
• W2003906068 hasConcept C161790260 @default.
• W2003906068 hasConcept C168056786 @default.
• W2003906068 hasConcept C175234220 @default.
• W2003906068 hasConcept C178790620 @default.
• W2003906068 hasConcept C185592680 @default.
• W2003906068 hasConcept C192562407 @default.
• W2003906068 hasConcept C2776345496 @default.
• W2003906068 hasConcept C2777207669 @default.
• W2003906068 hasConcept C2778717364 @default.
• W2003906068 hasConcept C2779681308 @default.
• W2003906068 hasConcept C2780471494 @default.
• W2003906068 hasConcept C42360764 @default.
• W2003906068 hasConcept C44280652 @default.
• W2003906068 hasConcept C64768522 @default.
• W2003906068 hasConcept C78762247 @default.
• W2003906068 hasConcept C97355855 @default.
• W2003906068 hasConceptScore W2003906068C121332964 @default.
• W2003906068 hasConceptScore W2003906068C127172972 @default.
• W2003906068 hasConceptScore W2003906068C127313418 @default.
• W2003906068 hasConceptScore W2003906068C127413603 @default.
• W2003906068 hasConceptScore W2003906068C131779963 @default.
• W2003906068 hasConceptScore W2003906068C159985019 @default.
• W2003906068 hasConceptScore W2003906068C161790260 @default.
• W2003906068 hasConceptScore W2003906068C168056786 @default.
• W2003906068 hasConceptScore W2003906068C175234220 @default.
• W2003906068 hasConceptScore W2003906068C178790620 @default.
• W2003906068 hasConceptScore W2003906068C185592680 @default.
• W2003906068 hasConceptScore W2003906068C192562407 @default.
• W2003906068 hasConceptScore W2003906068C2776345496 @default.
• W2003906068 hasConceptScore W2003906068C2777207669 @default.
• W2003906068 hasConceptScore W2003906068C2778717364 @default.
• W2003906068 hasConceptScore W2003906068C2779681308 @default.
• W2003906068 hasConceptScore W2003906068C2780471494 @default.
• W2003906068 hasConceptScore W2003906068C42360764 @default.
• W2003906068 hasConceptScore W2003906068C44280652 @default.
• W2003906068 hasConceptScore W2003906068C64768522 @default.
• W2003906068 hasConceptScore W2003906068C78762247 @default.
• W2003906068 hasConceptScore W2003906068C97355855 @default.
• W2003906068 hasLocation W20039060681 @default.
• W2003906068 hasOpenAccess W2003906068 @default.
• W2003906068 hasPrimaryLocation W20039060681 @default.
• W2003906068 hasRelatedWork W1197106166 @default.

• next