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pro vyhledávání: '"Benoit Fillion"'
Publikováno v:
Chemical Engineering and Processing: Process Intensification. 42:621-643
Almost all available literature correlations to predict the volumetric gas–liquid mass transfer coefficient, kLa in agitated reactors are systems- or operating conditions-dependent. In this study, two back-propagation neural networks (BPNNs), one d
Publikováno v:
Industrial & Engineering Chemistry Research. 41:697-709
The kinetics for soybean oil hydrogenation using a commercial Ni/Al2O3 catalyst were investigated in a 2 × 10-3 m3 agitated reaction calorimeter operating under a wide range of temperatures (383−44...
Autor:
Badie I. Morsi, Benoit Fillion and
Publikováno v:
Industrial & Engineering Chemistry Research. 39:2157-2168
This paper presents some experimental data on the volumetric gas−liquid mass-transfer coefficient (kLa), liquid-side mass-transfer coefficient (kL), gas−liquid interfacial area (a), bubble Sauter m...
Publikováno v:
International Journal of Chemical Reactor Engineering. 2
The critical mixing speed for gas entrainment (NCRE), for gas induction (NCRI), induced gas flow rate (QGI) as well as the wavy gas-liquid interfacial area (aWave) of N2 and air were measured in pure toluene and three mixtures of organic liquids (tol