Simulation of particles and gas flow behavior in the riser section of a circulating fluidized bed using the kinetic theory approach for the particulate phase S Benyahia, H Arastoopour, TM Knowlton, H Massah Powder Technology 112 (1-2), 24-33, 2000 | 425 | 2000 |
Extension of Hill–Koch–Ladd drag correlation over all ranges of Reynolds number and solids volume fraction S Benyahia, M Syamlal, TJ O'Brien Powder Technology 162 (2), 166-174, 2006 | 232 | 2006 |
Evaluation of boundary conditions used to model dilute, turbulent gas/solids flows in a pipe S Benyahia, M Syamlal, TJ O'Brien Powder Technology 156 (2-3), 62-72, 2005 | 210 | 2005 |
Study of the ability of multiphase continuum models to predict core‐annulus flow S Benyahia, M Syamlal, TJ O'Brien AIChE Journal 53 (10), 2549-2568, 2007 | 174 | 2007 |
MP-PIC simulation of CFB riser with EMMS-based drag model F Li, F Song, S Benyahia, W Wang, J Li Chemical Engineering Science 82, 104-113, 2012 | 154 | 2012 |
Revisiting Johnson and Jackson boundary conditions for granular flows T Li, S Benyahia AIChE journal 58 (7), 2058-2068, 2012 | 121 | 2012 |
Validation studies on filtered model equations for gas-particle flows in risers Y Igci, S Pannala, S Benyahia, S Sundaresan Industrial & Engineering Chemistry Research 51 (4), 2094-2103, 2012 | 114 | 2012 |
Extension of a coarse grained particle method to simulate heat transfer in fluidized beds L Lu, A Morris, T Li, S Benyahia International Journal of Heat and Mass Transfer 111, 723-735, 2017 | 108 | 2017 |
Estimation of numerical errors related to some basic assumptions in discrete particle methods S Benyahia, JE Galvin Industrial & Engineering Chemistry Research 49 (21), 10588-10605, 2010 | 108 | 2010 |
Do we need sub-grid scale corrections for both continuum and discrete gas-particle flow models? S Benyahia, S Sundaresan Powder Technology 220, 2-6, 2012 | 93 | 2012 |
On the effect of subgrid drag closures S Benyahia Industrial & Engineering Chemistry Research 49 (11), 5122-5131, 2010 | 91 | 2010 |
Summary of MFIX equations 2012-1 S Benyahia, M Syamlal, TJ O’Brien From URL https://mfix. netl. doe. gov/documentation/MFIXEquations2012-1. pdf …, 2012 | 89 | 2012 |
The effect of cohesive forces on the fluidization of aeratable powders JE Galvin, S Benyahia AIChE Journal 60 (2), 473-484, 2014 | 84 | 2014 |
Influence of grid resolution, parcel size and drag models on bubbling fluidized bed simulation L Lu, A Konan, S Benyahia Chemical Engineering Journal 326, 627-639, 2017 | 80 | 2017 |
Validation study of two continuum granular frictional flow theories S Benyahia Industrial & engineering chemistry research 47 (22), 8926-8932, 2008 | 77 | 2008 |
Analysis of model parameters affecting the pressure profile in a circulating fluidized bed S Benyahia AIChE Journal 58 (2), 427-439, 2012 | 76 | 2012 |
Coarse-grained-particle method for simulation of liquid–solids reacting flows L Lu, K Yoo, S Benyahia Industrial & Engineering Chemistry Research 55 (39), 10477-10491, 2016 | 75 | 2016 |
Assessment of different discrete particle methods ability to predict gas-particle flow in a small-scale fluidized bed L Lu, B Gopalan, S Benyahia Industrial & Engineering Chemistry Research 56 (27), 7865-7876, 2017 | 69 | 2017 |
Assessment of different coarse graining strategies to simulate polydisperse gas-solids flow L Lu, Y Xu, T Li, S Benyahia Chemical Engineering Science 179, 53-63, 2018 | 67 | 2018 |
Evaluation of wall boundary condition parameters for gas–solids fluidized bed simulations T Li, S Benyahia AIChE Journal 59 (10), 3624-3632, 2013 | 63 | 2013 |