## Abstract New data of gas‐liquid mass transfer for cocurrent downflow through packed beds of non‐porous particles are presented. Mass transfer parameters for air/carbon dioxide/water and air/carbon dioxide/sodium hydroxide systems were evaluated by least squares fit of the calculated CO~2~ concen
✦ LIBER ✦
Gas−Liquid Interfacial Mass Transfer in Trickle-Bed Reactors at Elevated Pressures
✍ Scribed by Larachi, F.; Cassanello, M.; Laurent, A.
- Book ID
- 120337150
- Publisher
- American Chemical Society
- Year
- 1998
- Tongue
- English
- Weight
- 212 KB
- Volume
- 37
- Category
- Article
- ISSN
- 0888-5885
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Mass transfer rates were determined in a 3.4cm id. trickle-bed reactor in the absence of reaction by absorption measurements and in presence of reaction. Gas flow rates were varied from O-100 I/h and liquid flow rates from O-l.5 I/h. The catalyst particles were crushed to an average diameter of 0.05