Jump to ContentJump to Main Navigation

New Journal at De Gruyter!

International Journal of Chemical Reactor Engineering

Ed. by de Lasa, Hugo / Xu, Charles Chunbao

4 Issues per year

IMPACT FACTOR 2013: 0.584

SCImago Journal Rank (SJR): 0.303
Source Normalized Impact per Paper (SNIP): 0.426

Flow Study and Wetting Efficiency of a Perforated-Plate Tray Distributor in a Trickle Bed Reactor

Damian Enrique Ramajo1 / Santiago Marquez Damian2 / Marcela Raviculé3 / Maria M. Monsalvo4 / Mario Storti5 / Norberto Nigro6

1Centro Internacional de Métodos Computacionales en Ingeniería,

2Centro Internacional de Métodos Computacionales en Ingeniería,

3Repsol YPF,

4Repsol YPF,

5Centro Internacional de Métodos Computacionales en Ingeniería,

6Centro Internacional de Métodos Computacionales en Ingeniería,

Citation Information: International Journal of Chemical Reactor Engineering. Volume 8, Issue 1, ISSN (Online) 1542-6580, DOI: 10.2202/1542-6580.2309, September 2010

Publication History

Published Online:

In this work, a computational fluid dynamics analysis (CFD) employing the Eulerian two-fluid model was carried out with the aim to understand the distribution process and to determine the wetting efficiency of the primary tray distributor (perforated plate) of a trickle bed reactor (TBR) under several operating conditions. The overall inlet geometry was considered, and the small holes of the perforated plate were modeled by sinks (drains) and sources, employing CFD and experimental models to obtain the hole discharge flow coefficients. The influence of the ceramic-ball bed above the catalyst bed was considered by a suitable correlation to estimate liquid distribution inside it.Results showed that because of the scarce liquid sloshing above the tray, little difference on liquid flow rate through the tray holes was found. Due to the really low inlet mass flow rate of gas, it has negligible influence on liquid behavior, which drops through holes slowly without spraying. Thus, the ceramic-ball bed above the catalyst bed is exclusively wetted in a small area under the tray holes. Although the ceramic-ball bed improves liquid distribution, which guarantees a minimum liquid volume fraction at all places, significant differences on the liquid mass flow rate across the top of the catalyst bed were found. Additional causes of low efficiency in TBR like the well-known fouling vulnerability of perforated-plate trays and unevenness were analyzed. For the first, two simple modifications were proposed to improve tray performance: reducing the amount of gas chimneys to only one and adding additional drip points and replacing the tray holes by short risers in order to avoid plugging.

Keywords: trickle bed reactors; CFD; tray efficiency; liquid distribution

Comments (0)

Please log in or register to comment.