Flow frictional resistance in pneumatic conveying of solid particles through inclined lines

Basit Öğe Kaydı
dc.authorid0000-0001-9055-1508en_US
dc.contributor.authorÇarpınlıoğlu, Melda Ö.
dc.contributor.authorÖzbelge, Tülay A.
dc.contributor.authorOruç, V.
dc.date.accessioned2024-02-26T12:24:28Z
dc.date.available2024-02-26T12:24:28Z
dc.date.issued2002en_US
dc.departmentDicle Üniversitesi, Mühendislik Fakültesi, Makine Mühendisliği Bölümüen_US
dc.description4th International Conference on Mulitphase Flow (ICMF-2001) May 27-Jun 01, 2001en_US
dc.description.abstractThe frictional behaviour of fully suspended dilute flow of granular solid particles in air through the transport lines of various angularities, α, with the horizontal plane in the range of 0°≤α≤30° is presented in this paper. The friction factor determination is based on the measurements of local static pressure gradients. The experiments were mainly directed to determine the effects of transport line inclination, particle physical characteristics, the ratio of mass flow rate of particles to that of air, Mp/Ma, and the flow Reynolds number, Re, on the two-phase friction factor. A variety of solid particles whose average diameter, dp, and apparent density, ρp, being in the respective ranges of 75.5 μm≤dp≤275 μm and 467.95 kg/m3≤ρp≤824.17 kg/m3 were used, with 5%≤Mp/Ma≤30%, at 50 000≤Re≤100 000, for this purpose. The results were expressed in terms of two-phase friction factor, fp+a, correlations proposed under the light of the state of art. The experimental data was also evaluated via solids friction factor, fs, correlated previously by Özbelge [Int. J. Multiphase Flow 10 (1984) 459] based on a theoretical analysis of vertical upward flow fields [Int. J. Multiphase Flow 9 (1983) 437] as well as to confirm the validity of the method in non-vertical upward flows.en_US
dc.identifier.citationÇarpınlıoğlu, M.Ö., Özbelge, T.A. ve Oruç, V. (2002). Flow frictional resistance in pneumatic conveying of solid particles through inclined lines. Powder Technology, 125(2-3), 292-297.en_US
dc.identifier.doi10.1016/S0032-5910(01)00517-4
dc.identifier.endpage297en_US
dc.identifier.issn0032-5910
dc.identifier.issue2-3en_US
dc.identifier.scopus2-s2.0-0037062531
dc.identifier.scopusqualityQ1
dc.identifier.startpage292en_US
dc.identifier.urihttps://www.sciencedirect.com/science/article/pii/S0032591001005174?via%3Dihub
dc.identifier.urihttps://hdl.handle.net/11468/13388
dc.identifier.volume125en_US
dc.identifier.wosWOS:000176536500023
dc.identifier.wosqualityQ1
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.institutionauthorOruç, Vedat
dc.language.isoenen_US
dc.publisherElsevieren_US
dc.relation.ispartofPowder Technology
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/restrictedAccessen_US
dc.subjectTwo-phase friction factoren_US
dc.subjectStatic pressure gradienten_US
dc.subjectTransport line angularityen_US
dc.titleFlow frictional resistance in pneumatic conveying of solid particles through inclined linesen_US
dc.titleFlow frictional resistance in pneumatic conveying of solid particles through inclined lines
dc.typeArticleen_US

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