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Wyszukujesz frazę "liquid holdup" wg kryterium: Temat


Wyświetlanie 1-2 z 2
Tytuł:
Numerical simulation of two-phase gas-liquid flow through horizontal annulus pipe
Autorzy:
Nyong, Oku E.
Igbong, Dodeye
Ebieto, Celestine
Ene, Bassey Ekpo
Oluwadare, Benjamin
Eso, Archibong Archibong
Tematy:
elongated bubble flow
gas-liquid two-phase flow
liquid holdup
PDF
annulus pipe
CFD modelling
Pokaż więcej
Wydawca:
Polska Akademia Nauk. Czasopisma i Monografie PAN
Powiązania:
https://bibliotekanauki.pl/articles/59112053.pdf  Link otwiera się w nowym oknie
Opis:
Chemical, petroleum and nuclear systems are only a few of the industrial processes that utilize gas-liquid flow in annular closed channels. However, concentric horizontal annuli flow patterns have received little attention. The ability to precisely characterize two-phase flow patterns using computational techniques is crucial for the production, transportation, and optimization of designs. This current research aims to establish the accuracy of the computational fluid dynamics (CFD) model in predicting the gas-liquid flow pattern in the concentric annulus pipe and validating the flow pattern of liquid holdup with experimental results from the literature. The simulations were done on a test section of a 12.8 m length pipe with a hydraulic diameter of 0.0168 m using air and water as the working fluids. The volume of fluid (VOF) model in Ansys Fluent based on the Eulerian- Eulerian approach in conjunction with the realizable k-ε turbulence model was used to model the gas-liquid flow pattern, i.e. dispersed bubble, elongated bubble, and slug in a horizontal annulus. A comparison of the model with the experimental high-speed video images shows a reasonable agreement for the flow pattern and liquid holdup data.
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Parametric sensitivity of a CFD model concerning the hydrodynamics of trickle-bed reactor (TBR)
Autorzy:
Janecki, D.
Burghardt, A.
Bartelmus, G.
Tematy:
hydrodynamics
trickle-flow regime
pressure gradient
liquid holdup
phases interaction
CFD
hydrodynamika
gradient ciśnienia
Pokaż więcej
Wydawca:
Polska Akademia Nauk. Czasopisma i Monografie PAN
Powiązania:
https://bibliotekanauki.pl/articles/184944.pdf  Link otwiera się w nowym oknie
Opis:
The aim of the present study was to investigate the sensitivity of a multiphase Eulerian CFD model with respect to relations defining drag forces between phases. The mean relative error as well as standard deviation of experimental and computed values of pressure gradient and average liquid holdup were used as validation criteria of the model. Comparative basis for simulations was our own data-base obtained in experiments carried out in a TBR operating at a co-current downward gas and liquid flow. Estimated errors showed that the classical equations of Attou et al. (1999) defining the friction factors Fjk approximate experimental values of hydrodynamic parameters with the best agreement. Taking this into account one can recommend to apply chosen equations in the momentum balances of TBR.
Dostawca treści:
Biblioteka Nauki
Artykuł
    Wyświetlanie 1-2 z 2

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