Zobrazeno 1 - 10
of 19
pro vyhledávání: '"Hamza Albazzaz"'
Autor:
Narjes Ghaloum, Muhieddine A. Safa, Hamza Albazzaz, Mohammed S. Alshemali, Shibu Jose, Xiaoliang Ma
Publikováno v:
ACS Omega, Vol 9, Iss 39, Pp 41011-41020 (2024)
Externí odkaz:
https://doaj.org/article/407c2f0f36004c1fb15e21ce0b5b0505
Publikováno v:
ChemEngineering, Vol 8, Iss 3, p 54 (2024)
This study explores the dynamics of liquid holdup in a lab-scale co-current two-phase upflow moving packed bed reactor, specifically examining how superficial gas velocity influences the line average external liquid holdup at a fixed superficial liqu
Externí odkaz:
https://doaj.org/article/678324fc8b96463e8124f16341bf3c9e
Publikováno v:
Catalysis Today. 371:258-264
Effects of co-existing nitrogen compounds and polycyclic aromatic hydrocarbons (PAH) on oxidative desulfurization (ODS) of middle distillates with cumene hydroperoxide over a MoO3/Al2O3 catalyst were quantitatively studied by using three different fe
Publikováno v:
The Canadian Journal of Chemical Engineering. 99:1558-1569
Publikováno v:
Chemical Engineering Communications. 208:1725-1736
A mathematical model for the atmospheric residue desulfurization (ARDS) process was used to estimate the deactivation parameters for the hydrodesulfurization (HDS) and hydrodemetalation (HDM) react...
Publikováno v:
Catalysis Today. 329:125-134
Recently, significant changes in petroleum sources have been observed where light crude sources are becoming heavy or extra heavy, containing a large number of contaminants (S, N, metals, asphaltene, etc.), and producing a significant fraction of the
Publikováno v:
Chemical Engineering Science. 195:671-682
Gas dispersion studies has been executed for the catalyst bed section of a representative geometry of scaled-down industrial Moving Bed Hydrotreater Reactor (MBR). The catalyst bed of MBR is modeled using Axial Dispersion Model (ADM) and its paramete
Liquid phase dispersion/mixing studies have been performed for the first time on the catalyst bed of a cold flow scaled-down upflow moving bed re- actor (MBR) using residence time distribution (RTD) at various flow rates including the scaled down con
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2fcc8f29ad26eba0c80762c97840e4a2
https://doi.org/10.22541/au.158940721.14994592
https://doi.org/10.22541/au.158940721.14994592
Publikováno v:
Energy & Fuels. 32:5480-5488
The effect of three atmospheric residual oils on the deactivation of a commercial atmospheric residue desulfurization (ARDS) catalyst system was assessed using a commercial catalyst system consisting of five catalysts loaded inside a two-reactor pilo