Ministry of Science and Technological Development (Republic of Serbia)

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Ministry of Science and Technological Development (Republic of Serbia)

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Numerical model of gaseous fuel jet injection into a fluidized furnace

Nemoda, Stevan; Mladenović, Milica R.; Belošević, Srđan; Mladenovic, Rastko; Dakić, Dragoljub V.

(2009)

TY  - JOUR
AU  - Nemoda, Stevan
AU  - Mladenović, Milica R.
AU  - Belošević, Srđan
AU  - Mladenovic, Rastko
AU  - Dakić, Dragoljub V.
PY  - 2009
UR  - https://vinar.vin.bg.ac.rs/handle/123456789/3726
AB  - The paper presents a fluid-porous medium model, developed for stationary 2D predictions of fluidized bed. Dense phase is considered a fixed porous medium, while gas-particle interactions and bubbling phase are modeled regarding balance of friction forces between gas and particles. Like referent measurements, predictions of lateral jet injection into the bed suggest the jet penetration length is strongly affected by fluid velocity at the nozzle outlet, while influences of the nozzle vertical position and inclination angle are not significant. Also, the fluid velocity and the nozzle vertical position exert pronounced effects on mixing rate of components (fuel and oxidizer). (C) 2009 Elsevier Ltd. All rights reserved.
T2  - International Journal of Heat and Mass Transfer
T1  - Numerical model of gaseous fuel jet injection into a fluidized furnace
VL  - 52
IS  - 15-16
SP  - 3427
EP  - 3438
DO  - 10.1016/j.ijheatmasstransfer.2009.02.045
ER  - 
@article{
author = "Nemoda, Stevan and Mladenović, Milica R. and Belošević, Srđan and Mladenovic, Rastko and Dakić, Dragoljub V.",
year = "2009",
abstract = "The paper presents a fluid-porous medium model, developed for stationary 2D predictions of fluidized bed. Dense phase is considered a fixed porous medium, while gas-particle interactions and bubbling phase are modeled regarding balance of friction forces between gas and particles. Like referent measurements, predictions of lateral jet injection into the bed suggest the jet penetration length is strongly affected by fluid velocity at the nozzle outlet, while influences of the nozzle vertical position and inclination angle are not significant. Also, the fluid velocity and the nozzle vertical position exert pronounced effects on mixing rate of components (fuel and oxidizer). (C) 2009 Elsevier Ltd. All rights reserved.",
journal = "International Journal of Heat and Mass Transfer",
title = "Numerical model of gaseous fuel jet injection into a fluidized furnace",
volume = "52",
number = "15-16",
pages = "3427-3438",
doi = "10.1016/j.ijheatmasstransfer.2009.02.045"
}
Nemoda, S., Mladenović, M. R., Belošević, S., Mladenovic, R.,& Dakić, D. V.. (2009). Numerical model of gaseous fuel jet injection into a fluidized furnace. in International Journal of Heat and Mass Transfer, 52(15-16), 3427-3438.
https://doi.org/10.1016/j.ijheatmasstransfer.2009.02.045
Nemoda S, Mladenović MR, Belošević S, Mladenovic R, Dakić DV. Numerical model of gaseous fuel jet injection into a fluidized furnace. in International Journal of Heat and Mass Transfer. 2009;52(15-16):3427-3438.
doi:10.1016/j.ijheatmasstransfer.2009.02.045 .
Nemoda, Stevan, Mladenović, Milica R., Belošević, Srđan, Mladenovic, Rastko, Dakić, Dragoljub V., "Numerical model of gaseous fuel jet injection into a fluidized furnace" in International Journal of Heat and Mass Transfer, 52, no. 15-16 (2009):3427-3438,
https://doi.org/10.1016/j.ijheatmasstransfer.2009.02.045 . .
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