FRINK Linked Data Fragments server

Matches in SemOpenAlex for { <https://semopenalex.org/work/W1969962766> ?p ?o ?g. }

• W1969962766 endingPage "5808" @default.
• W1969962766 startingPage "5794" @default.
• W1969962766 abstract "In this study is presented a general methodology to predict the performance of a continuous near-critical fluid extraction process to remove compounds from aqueous solutions using a hollow fiber membrane contactor. The stabilization of the gas–liquid interface in the membrane porosity and a high surface area to contact both phases represent some of the advantages that hollow fiber contactors offer over conventional contactor devices for the extraction of compounds from liquid feeds. A mathematical model has been developed integrating a resistances-in-series mass transfer system that takes into account boundary layers, membrane porosity and thermodynamic considerations with mass balances of the membrane contactor. Simulation algorithms were easily implemented with low calculation requirements. The system studied in this work is a membrane based extractor of ethanol and acetone from aqueous solutions using near-critical CO2. Predictions of extraction percentages obtained by simulations have been compared to the experimental values reported by Bothun et al. [2003a. Compressed solvents for the extraction of fermentation products within a hollow fiber membrane contactor. Journal of Supercritical Fluids 25, 119–134]. Simulations of extraction percentage of ethanol and acetone show an average difference of 36.3% and 6.75% with the experimental data, respectively. More accurate predictions of the extraction of acetone could be explained by a better estimation of the transport properties in the aqueous phase that controls the extraction of this solute. When the model was validated, the effect of the configuration and the operating parameters was studied and local mass transfer resistances were evaluated. The proposed approach allows the evaluation of the relevance of membrane hydrophobicity for extraction in solutions under different thermodynamic conditions. This original methodology based on well-known phenomenological equations represents a general approach which could be applied in other processes using membrane contactors with different configurations." @default.
• W1969962766 created "2016-06-24" @default.
• W1969962766 creator A5030004784 @default.
• W1969962766 creator A5034653669 @default.
• W1969962766 creator A5041765554 @default.
• W1969962766 creator A5043725540 @default.
• W1969962766 creator A5063427042 @default.
• W1969962766 creator A5091028297 @default.
• W1969962766 date "2007-11-01" @default.
• W1969962766 modified "2023-09-26" @default.
• W1969962766 title "Modeling and simulation of mass transfer in near-critical extraction using a hollow fiber membrane contactor" @default.
• W1969962766 cites W1963534566 @default.
• W1969962766 cites W1965116601 @default.
• W1969962766 cites W1973333262 @default.
• W1969962766 cites W1985019986 @default.
• W1969962766 cites W1987807167 @default.
• W1969962766 cites W2003090704 @default.
• W1969962766 cites W2005496208 @default.
• W1969962766 cites W2009942042 @default.
• W1969962766 cites W2015193572 @default.
• W1969962766 cites W2021977714 @default.
• W1969962766 cites W2027181910 @default.
• W1969962766 cites W2029097972 @default.
• W1969962766 cites W2034133890 @default.
• W1969962766 cites W2035415675 @default.
• W1969962766 cites W2037102425 @default.
• W1969962766 cites W2045308902 @default.
• W1969962766 cites W2048731981 @default.
• W1969962766 cites W2055632497 @default.
• W1969962766 cites W2073146624 @default.
• W1969962766 cites W2079234324 @default.
• W1969962766 cites W2085726336 @default.
• W1969962766 cites W2094815800 @default.
• W1969962766 cites W2098007393 @default.
• W1969962766 cites W2154407893 @default.
• W1969962766 cites W2161087927 @default.
• W1969962766 cites W3102239342 @default.
• W1969962766 doi "https://doi.org/10.1016/j.ces.2007.05.037" @default.
• W1969962766 hasPublicationYear "2007" @default.
• W1969962766 type Work @default.
• W1969962766 sameAs 1969962766 @default.
• W1969962766 citedByCount "24" @default.
• W1969962766 countsByYear W19699627662012 @default.
• W1969962766 countsByYear W19699627662013 @default.
• W1969962766 countsByYear W19699627662014 @default.
• W1969962766 countsByYear W19699627662015 @default.
• W1969962766 countsByYear W19699627662016 @default.
• W1969962766 countsByYear W19699627662017 @default.
• W1969962766 countsByYear W19699627662018 @default.
• W1969962766 countsByYear W19699627662019 @default.
• W1969962766 countsByYear W19699627662022 @default.
• W1969962766 crossrefType "journal-article" @default.
• W1969962766 hasAuthorship W1969962766A5030004784 @default.
• W1969962766 hasAuthorship W1969962766A5034653669 @default.
• W1969962766 hasAuthorship W1969962766A5041765554 @default.
• W1969962766 hasAuthorship W1969962766A5043725540 @default.
• W1969962766 hasAuthorship W1969962766A5063427042 @default.
• W1969962766 hasAuthorship W1969962766A5091028297 @default.
• W1969962766 hasConcept C101555633 @default.
• W1969962766 hasConcept C113196181 @default.
• W1969962766 hasConcept C121332964 @default.
• W1969962766 hasConcept C147789679 @default.
• W1969962766 hasConcept C159985019 @default.
• W1969962766 hasConcept C163258240 @default.
• W1969962766 hasConcept C178790620 @default.
• W1969962766 hasConcept C184651966 @default.
• W1969962766 hasConcept C185592680 @default.
• W1969962766 hasConcept C192562407 @default.
• W1969962766 hasConcept C199919908 @default.
• W1969962766 hasConcept C2778260969 @default.
• W1969962766 hasConcept C2781213060 @default.
• W1969962766 hasConcept C41625074 @default.
• W1969962766 hasConcept C43617362 @default.
• W1969962766 hasConcept C4725764 @default.
• W1969962766 hasConcept C51038369 @default.
• W1969962766 hasConcept C55493867 @default.
• W1969962766 hasConcept C6648577 @default.
• W1969962766 hasConcept C78592999 @default.
• W1969962766 hasConcept C97355855 @default.
• W1969962766 hasConceptScore W1969962766C101555633 @default.
• W1969962766 hasConceptScore W1969962766C113196181 @default.
• W1969962766 hasConceptScore W1969962766C121332964 @default.
• W1969962766 hasConceptScore W1969962766C147789679 @default.
• W1969962766 hasConceptScore W1969962766C159985019 @default.
• W1969962766 hasConceptScore W1969962766C163258240 @default.
• W1969962766 hasConceptScore W1969962766C178790620 @default.
• W1969962766 hasConceptScore W1969962766C184651966 @default.
• W1969962766 hasConceptScore W1969962766C185592680 @default.
• W1969962766 hasConceptScore W1969962766C192562407 @default.
• W1969962766 hasConceptScore W1969962766C199919908 @default.
• W1969962766 hasConceptScore W1969962766C2778260969 @default.
• W1969962766 hasConceptScore W1969962766C2781213060 @default.
• W1969962766 hasConceptScore W1969962766C41625074 @default.
• W1969962766 hasConceptScore W1969962766C43617362 @default.
• W1969962766 hasConceptScore W1969962766C4725764 @default.
• W1969962766 hasConceptScore W1969962766C51038369 @default.
• W1969962766 hasConceptScore W1969962766C55493867 @default.
• W1969962766 hasConceptScore W1969962766C6648577 @default.

• next