Wall-to-bed heat transfer in vertical hydraulic transport and in particulate fluidized beds
Samo za registrovane korisnike
2008
Članak u časopisu (Objavljena verzija)
Metapodaci
Prikaz svih podataka o dokumentuApstrakt
Wall-to-bed heat transfer in hydraulic transport and in particulate fluidized beds of spherical particles was studied. Experiments were performed by spherical glass particles of 0.80-2.98 mm in diameter with water in a 25.4 mm I.D. cooper tube equipped with a steam jacket. In the hydraulic transport runs the Reynolds number varied between 3300 and 20150 (particles of 1.20,1.94 and 2.98 mm in diameter), while in particulate fluidized beds Reynolds number varied between 1960 and 7850 (particles of 0.80, 1.10 and 1.94 mm in diameter). The influence of different parameters as liquid velocity, particles size and voidage on heat transfer in fluidized beds and in hydraulic transport are presented. In our hydraulic transport experiments, the two characteristic flow regimes were observed: "turbulent" and "parallel" flow. Our experimental data show that the heat transfer coefficients in "turbulent" regime are much higher then in "parallel" flow, and the heat transfer coefficients is generally hi...gher while the flow is in fluidized bed. The data for heat transfer in particulate fluidized beds and for vertical hydraulic transport were correlated treating the flowing fluid-particle mixture as a pseudo fluid. New correlation for heat transfer factor in fluidized beds and in vertical hydraulic transport is proposed.
Ključne reči:
Liquid-solids / Heat transfer / Vertical transport / Fluidized bed / PseudofluidIzvor:
International Journal of Heat and Mass Transfer, 2008, 51, 25-26, 5942-5948Izdavač:
- Oxford : Pergamon-Elsevier Science Ltd
Finansiranje / projekti:
- Research Council of Serbia
DOI: 10.1016/j.ijheatmasstransfer.2008.03.030
ISSN: 0017-9310
WoS: 000261628800022
Scopus: 2-s2.0-55649099438
Institucija/grupa
IHTMTY - JOUR AU - Garić Grulović, Radmila AU - Bošković-Vragolović, Nevenka AU - Grbavčić, Željko AU - Arsenijević, Zorana PY - 2008 UR - https://cer.ihtm.bg.ac.rs/handle/123456789/387 AB - Wall-to-bed heat transfer in hydraulic transport and in particulate fluidized beds of spherical particles was studied. Experiments were performed by spherical glass particles of 0.80-2.98 mm in diameter with water in a 25.4 mm I.D. cooper tube equipped with a steam jacket. In the hydraulic transport runs the Reynolds number varied between 3300 and 20150 (particles of 1.20,1.94 and 2.98 mm in diameter), while in particulate fluidized beds Reynolds number varied between 1960 and 7850 (particles of 0.80, 1.10 and 1.94 mm in diameter). The influence of different parameters as liquid velocity, particles size and voidage on heat transfer in fluidized beds and in hydraulic transport are presented. In our hydraulic transport experiments, the two characteristic flow regimes were observed: "turbulent" and "parallel" flow. Our experimental data show that the heat transfer coefficients in "turbulent" regime are much higher then in "parallel" flow, and the heat transfer coefficients is generally higher while the flow is in fluidized bed. The data for heat transfer in particulate fluidized beds and for vertical hydraulic transport were correlated treating the flowing fluid-particle mixture as a pseudo fluid. New correlation for heat transfer factor in fluidized beds and in vertical hydraulic transport is proposed. PB - Oxford : Pergamon-Elsevier Science Ltd T2 - International Journal of Heat and Mass Transfer T1 - Wall-to-bed heat transfer in vertical hydraulic transport and in particulate fluidized beds VL - 51 IS - 25-26 SP - 5942 EP - 5948 DO - 10.1016/j.ijheatmasstransfer.2008.03.030 ER -
@article{ author = "Garić Grulović, Radmila and Bošković-Vragolović, Nevenka and Grbavčić, Željko and Arsenijević, Zorana", year = "2008", abstract = "Wall-to-bed heat transfer in hydraulic transport and in particulate fluidized beds of spherical particles was studied. Experiments were performed by spherical glass particles of 0.80-2.98 mm in diameter with water in a 25.4 mm I.D. cooper tube equipped with a steam jacket. In the hydraulic transport runs the Reynolds number varied between 3300 and 20150 (particles of 1.20,1.94 and 2.98 mm in diameter), while in particulate fluidized beds Reynolds number varied between 1960 and 7850 (particles of 0.80, 1.10 and 1.94 mm in diameter). The influence of different parameters as liquid velocity, particles size and voidage on heat transfer in fluidized beds and in hydraulic transport are presented. In our hydraulic transport experiments, the two characteristic flow regimes were observed: "turbulent" and "parallel" flow. Our experimental data show that the heat transfer coefficients in "turbulent" regime are much higher then in "parallel" flow, and the heat transfer coefficients is generally higher while the flow is in fluidized bed. The data for heat transfer in particulate fluidized beds and for vertical hydraulic transport were correlated treating the flowing fluid-particle mixture as a pseudo fluid. New correlation for heat transfer factor in fluidized beds and in vertical hydraulic transport is proposed.", publisher = "Oxford : Pergamon-Elsevier Science Ltd", journal = "International Journal of Heat and Mass Transfer", title = "Wall-to-bed heat transfer in vertical hydraulic transport and in particulate fluidized beds", volume = "51", number = "25-26", pages = "5942-5948", doi = "10.1016/j.ijheatmasstransfer.2008.03.030" }
Garić Grulović, R., Bošković-Vragolović, N., Grbavčić, Ž.,& Arsenijević, Z.. (2008). Wall-to-bed heat transfer in vertical hydraulic transport and in particulate fluidized beds. in International Journal of Heat and Mass Transfer Oxford : Pergamon-Elsevier Science Ltd., 51(25-26), 5942-5948. https://doi.org/10.1016/j.ijheatmasstransfer.2008.03.030
Garić Grulović R, Bošković-Vragolović N, Grbavčić Ž, Arsenijević Z. Wall-to-bed heat transfer in vertical hydraulic transport and in particulate fluidized beds. in International Journal of Heat and Mass Transfer. 2008;51(25-26):5942-5948. doi:10.1016/j.ijheatmasstransfer.2008.03.030 .
Garić Grulović, Radmila, Bošković-Vragolović, Nevenka, Grbavčić, Željko, Arsenijević, Zorana, "Wall-to-bed heat transfer in vertical hydraulic transport and in particulate fluidized beds" in International Journal of Heat and Mass Transfer, 51, no. 25-26 (2008):5942-5948, https://doi.org/10.1016/j.ijheatmasstransfer.2008.03.030 . .