CFD Simulation of Flue Gas Desulfurization
About This Video This video shows transient computational fluid dynamics model results for an industrial dry flue gas desulfurization system. A hot gas stream containing 200 PPM SO2 enters and…
About This Video This video shows transient computational fluid dynamics model results for an industrial dry flue gas desulfurization system. A hot gas stream containing 200 PPM SO2 enters and…
About This Video This video shows the transient, 3D modeling of the thermal and reacting flows inside an FCC riser located on the Arabian Peninsula. Ecat from the regenerator enters…
About This Video 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…
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.
Adding the current directory, also known as “.”, to your Linux systems PATH environment variable can make executing scripts more convenient. However, there are some security issues to consider as…
Barracuda VR 16.0.6 Issues affecting this version: KI-1: Particle Drag is not calculated for pure liquid particles when simulation has no solid materials KI-2: 2D data is missing output conversion…
Update – April 24, 2018 This version of Barracuda Virtual Reactor is no longer available for download. For the latest version of Virtual Reactor™, please visit the Dashboard. If you…
About This Video This video shows the transient engagement of densely-loaded spent FCC catalyst exiting from the standpipe into a lift riser for transport into an FCC regenerator. The bi-direction…