Zobrazeno 1 - 6
of 6
pro vyhledávání: '"Arsam Behkish"'
Autor:
Badie I. Morsi, Rachid Oukaci, Laurent Sehabiague, Romain Lemoine, Yannick J. Heintz, Arsam Behkish
Publikováno v:
Fuel Processing Technology. 89:322-343
A large number of experimental data points obtained in our laboratory as well as from the literature, covering wide ranges of reactor geometry (column diameter, gas distributor type/open area), physicochemical properties (liquid and gas densities and
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::c0ef21a2e1b9dd1a6c88b850cb3d463a
https://doi.org/10.1016/j.fuproc.2007.11.016
https://doi.org/10.1016/j.fuproc.2007.11.016
Autor:
Badie I. Morsi, Laurent Sehabiague, Yannick J. Heintz, Mariela Sanoja, Arsam Behkish, Romain Lemoine, Rachid Oukaci
Publikováno v:
Journal of the Chinese Institute of Chemical Engineers. 39:169-179
A user-friendly simulator based on a comprehensive computer model for slurry bubble column reactors (SBCRs) for Fischer–Tropsch (F–T) synthesis, taking into account the hydrodynamics, kinetics, heat transfer, and mass transfer was developed. The
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d4dd6f567ef36198a78aa1492b4adf0c
https://doi.org/10.1016/j.jcice.2007.11.003
https://doi.org/10.1016/j.jcice.2007.11.003
Publikováno v:
Chemical Engineering Journal. 128:69-84
The holdups of small and large gas bubbles, bubble size distribution and the Sauter-mean bubble diameter were measured for N 2 and He in isoparaffinic organic liquid mixture (Isopar-M) in the absence and presence of Alumina powder under various press
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::14a0f474e5290619ad32dac3af1806cb
https://doi.org/10.1016/j.cej.2006.10.016
https://doi.org/10.1016/j.cej.2006.10.016
Publikováno v:
Industrial & Engineering Chemistry Research. 43:6195-6212
The gas holdup (eG), Sauter mean bubble diameter (dS), and bubble size distribution, as well as the volumetric mass-transfer coefficient (kLa), gas−liquid interfacial area (a), and mass-transfer coefficient (kL), of N2 and air were measured in a la
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::73a84414491eb04e568d64c57ffe50bd
https://doi.org/10.1021/ie0400797
https://doi.org/10.1021/ie0400797
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
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::abc953890f5432c79233c1add9deb258
https://doi.org/10.1016/s0255-2701(02)00211-8
https://doi.org/10.1016/s0255-2701(02)00211-8
Publikováno v:
Chemical Engineering Science. 57:3307-3324
The mass transfer coefficients ( k L a ) and bubbles size distribution were measured in a large-scale (0.316-m inside diameter, 2.8-m high) slurry bubble column reactor (SBCR) for H 2 , CO, N 2 and CH 4 in two organic liquid mixtures (Isopar-M and a
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::128ac5f6e5e091f887c3e5d3d925fcaa
https://doi.org/10.1016/s0009-2509(02)00201-4
https://doi.org/10.1016/s0009-2509(02)00201-4