TY  - JOUR
AV  - none
N1  - cited By 1; Conference of International Conference on Process Engineering and Advanced Materials, ICPEAM 2012 ; Conference Date: 12 June 2012 Through 14 June 2012; Conference Code:106208
SP  - 267
TI  - Simulation of hydrodynamics and reaction behavior in an industrial RFCC riser
PB  - Trans Tech Publications Ltd
SN  - 10226680
EP  - 282
CY  - Kuala Lumpur
N2  - A 2D axi-symmetric, steady state and pressure-based model for the riser of an industrial RFCC unit was developed with ANSYS FLUENT in workbench 13.0. The Eulerian-Eulerian approach was applied to simulate the flow behavior of the two phases and the catalytic cracking reactions. The k-ε gas-solid turbulent flow per phase model was used, and the particle-level fluctuations are modeled in the framework of the kinetic theory of granular flow. Two different drag models were used separately to simulate the gas solid interaction in the riser fluidized bed. The 14- lump kinetic model was chosen to describe the complex catalytic cracking of the heavy residual feed stock. The particle volume fraction, velocity and temperature profiles, as well as product yields in the riser were analyzed and validated with results from open literature and the industrial RFCC plant data. © (2014) Trans Tech Publications, Switzerland.
ID  - scholars5186
KW  - Catalytic cracking; Cracks; Fluidized beds; Particles (particulate matter); Process engineering; Turbulence
KW  -  14-lump; ANSYS fluent; Eulerian-Eulerian approach; Gas-solid turbulent flows; Kinetic theory of granular flow; Particle volume fractions; RFCC; Riser
KW  -  Industry
Y1  - 2014///
JF  - Advanced Materials Research
A1  - Ahmed, A.
A1  - Maulud, A.
A1  - Ramasamy, M.
A1  - Keng, L.K.
A1  - Mahadzir, S.
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-84904036154&doi=10.4028%2fwww.scientific.net%2fAMR.917.267&partnerID=40&md5=79dc60ac44a9459a335e93d343b149b7
VL  - 917
ER  -