FRINK Linked Data Fragments server

Matches in SemOpenAlex for { <https://semopenalex.org/work/W2805911018> ?p ?o ?g. }

• W2805911018 endingPage "196" @default.
• W2805911018 startingPage "187" @default.
• W2805911018 abstract "In this work, viscosity measurements of the ternary mixture [0.6511CH4 + 0.0808C3H8 + 0.2681CO2] were made over the temperature range (203–420) K and at pressures up to 31 MPa, with a combined overall standard uncertainty of 2.5%. The presence of CO2 or propane in the ternary mixture was found to always increase the viscosity relative to the constituent binary mixtures with larger differences observed at the highest density conditions: adding 26.8% mole fraction of CO2 to the binary mixture [xCH4 + (1−x)C3H8] with x = 0.8888, increased the viscosity by up to 45%. Similarly, adding 8.1% mole fraction of propane to the binary mixture [xCH4 + (1−x)CO2] with x = 0.7084, increased the viscosity by up to 23%; in this case, while the effect was apparent at lower temperatures, it was negligible at 370 K and above. The ternary mixture data were compared with the predictions of five models: corresponding states based approaches (ECS, SuperTRAPP and PFCT), the LBC model used widely by petroleum engineers, and a model (LJ) based on molecular dynamics simulations of Lennard Jones fluids. The relative deviations of the measured viscosities from those calculated by the five models exhibited a similar, systematic dependence on density, with stronger and larger systematic relative deviations observed at the lowest temperatures. The average absolute deviations from the measured viscosities were 2.5%, 6.4%, 8.0%, 4.2% and 3.9% for the ECS, ST, PFCT, LBC and LJ models respectively, with the ECS model providing a better representation of the data over the entire range. The present study reveals how well various engineering models can describe the viscosity of a multi-component mixture under supercritical conditions, which are of increasing interest in the energy industrial sector." @default.
• W2805911018 created "2018-06-13" @default.
• W2805911018 creator A5013018945 @default.
• W2805911018 creator A5031975844 @default.
• W2805911018 creator A5047183934 @default.
• W2805911018 date "2018-11-01" @default.
• W2805911018 modified "2023-10-15" @default.
• W2805911018 title "Viscosity measurements of (CH4 + C3H8 + CO2) mixtures at temperatures between (203 and 420) K and pressures between (3 and 31) MPa" @default.
• W2805911018 cites W19651616 @default.
• W2805911018 cites W1969315613 @default.
• W2805911018 cites W1969537408 @default.
• W2805911018 cites W1973084505 @default.
• W2805911018 cites W1975169001 @default.
• W2805911018 cites W1987341437 @default.
• W2805911018 cites W1997041206 @default.
• W2805911018 cites W2011071169 @default.
• W2805911018 cites W2014356251 @default.
• W2805911018 cites W2018249864 @default.
• W2805911018 cites W2020412643 @default.
• W2805911018 cites W2020616432 @default.
• W2805911018 cites W2026141921 @default.
• W2805911018 cites W2028660200 @default.
• W2805911018 cites W2032744801 @default.
• W2805911018 cites W2034133890 @default.
• W2805911018 cites W2039660394 @default.
• W2805911018 cites W2057163258 @default.
• W2805911018 cites W2058460659 @default.
• W2805911018 cites W2059338364 @default.
• W2805911018 cites W2062264174 @default.
• W2805911018 cites W2062711966 @default.
• W2805911018 cites W2070472828 @default.
• W2805911018 cites W2077738176 @default.
• W2805911018 cites W2079739853 @default.
• W2805911018 cites W2093185348 @default.
• W2805911018 cites W2093556696 @default.
• W2805911018 cites W2105762977 @default.
• W2805911018 cites W2131372637 @default.
• W2805911018 cites W2314256432 @default.
• W2805911018 cites W2327831005 @default.
• W2805911018 cites W2334895876 @default.
• W2805911018 cites W2412589109 @default.
• W2805911018 cites W2464727966 @default.
• W2805911018 cites W2507394595 @default.
• W2805911018 cites W2735026210 @default.
• W2805911018 cites W2792736995 @default.
• W2805911018 cites W2795842109 @default.
• W2805911018 cites W4300497458 @default.
• W2805911018 cites W62711388 @default.
• W2805911018 doi "https://doi.org/10.1016/j.fuel.2018.05.087" @default.
• W2805911018 hasPublicationYear "2018" @default.
• W2805911018 type Work @default.
• W2805911018 sameAs 2805911018 @default.
• W2805911018 citedByCount "13" @default.
• W2805911018 countsByYear W28059110182019 @default.
• W2805911018 countsByYear W28059110182020 @default.
• W2805911018 countsByYear W28059110182021 @default.
• W2805911018 countsByYear W28059110182023 @default.
• W2805911018 crossrefType "journal-article" @default.
• W2805911018 hasAuthorship W2805911018A5013018945 @default.
• W2805911018 hasAuthorship W2805911018A5031975844 @default.
• W2805911018 hasAuthorship W2805911018A5047183934 @default.
• W2805911018 hasConcept C113196181 @default.
• W2805911018 hasConcept C121332964 @default.
• W2805911018 hasConcept C127172972 @default.
• W2805911018 hasConcept C169820759 @default.
• W2805911018 hasConcept C185592680 @default.
• W2805911018 hasConcept C18762648 @default.
• W2805911018 hasConcept C199360897 @default.
• W2805911018 hasConcept C2776345496 @default.
• W2805911018 hasConcept C33923547 @default.
• W2805911018 hasConcept C36591836 @default.
• W2805911018 hasConcept C41008148 @default.
• W2805911018 hasConcept C43617362 @default.
• W2805911018 hasConcept C48372109 @default.
• W2805911018 hasConcept C64452783 @default.
• W2805911018 hasConcept C94375191 @default.
• W2805911018 hasConcept C97355855 @default.
• W2805911018 hasConceptScore W2805911018C113196181 @default.
• W2805911018 hasConceptScore W2805911018C121332964 @default.
• W2805911018 hasConceptScore W2805911018C127172972 @default.
• W2805911018 hasConceptScore W2805911018C169820759 @default.
• W2805911018 hasConceptScore W2805911018C185592680 @default.
• W2805911018 hasConceptScore W2805911018C18762648 @default.
• W2805911018 hasConceptScore W2805911018C199360897 @default.
• W2805911018 hasConceptScore W2805911018C2776345496 @default.
• W2805911018 hasConceptScore W2805911018C33923547 @default.
• W2805911018 hasConceptScore W2805911018C36591836 @default.
• W2805911018 hasConceptScore W2805911018C41008148 @default.
• W2805911018 hasConceptScore W2805911018C43617362 @default.
• W2805911018 hasConceptScore W2805911018C48372109 @default.
• W2805911018 hasConceptScore W2805911018C64452783 @default.
• W2805911018 hasConceptScore W2805911018C94375191 @default.
• W2805911018 hasConceptScore W2805911018C97355855 @default.
• W2805911018 hasLocation W28059110181 @default.
• W2805911018 hasOpenAccess W2805911018 @default.
• W2805911018 hasPrimaryLocation W28059110181 @default.
• W2805911018 hasRelatedWork W1981361459 @default.
• W2805911018 hasRelatedWork W1983164082 @default.

• next