CFD Simulation of Flue Gas Desulfurization
This video shows transient computational fluid dynamics model results for an industrial dry flue gas desulfurization system.
This video shows transient computational fluid dynamics model results for an industrial dry flue gas desulfurization system.
This video shows the transient, 3D modeling of the thermal and reacting flows inside an FCC riser located on the Arabian Peninsula.
A model of a full-scale fluidized catalytic cracking (FCC) regenerator using the Eulerian-Lagrangian CPFD method in Barracuda VR. This video illustrates the use of the Barracuda Virtual Reactor to predict the 100°F afterburn observed at the refinery.
Multiphase flow simulations created using Barracuda Virtual Reactor are used to compare with experimental data for determining minimum fluidization velocity for four different sizes of particles.
Fluidized beds are susceptible to such problems as bed slugging, loss of fines, and gas bypassing. This article explains how to avoid these pitfalls.
This paper presents a constitutive equation for the thermal heat transfer associated by mass transfer, applicable to both Eulerian–Eulerian and Eulerian–Lagrangian multiphase computational fluid dynamic models.
Fluidized beds offer excellent heat transfer, and have the unique ability to move a wide range of solid particles in a fluid-like fashion.
This study by researchers from the Shanghai Engineering Research Center of Coal Gasification investigated the applicability of the CPFD) numerical scheme for simulating flows in a 3-D hopper.
Bigda, from the Institute for Chemical Processing of Coal (IChPW), Poland, presents CPFD numerical studies of the hydrodynamics of gas-solid flow and the drying process using Barracuda Virtual Reactor.
In this paper a CPFD model for dry flue gas desulfurization (DFGD) systems was developed, validated against lab-scale data, and applied to an industrial-scale unit.