I can’t view my results in GMV anymore. What can I do?
There are various reasons that GMV output files (named Gmv.#####) may be unreadable by GMV. The three most common reasons are listed below: 1. Filled hard drive. This is more…
There are various reasons that GMV output files (named Gmv.#####) may be unreadable by GMV. The three most common reasons are listed below: 1. Filled hard drive. This is more…
In this study by Bioenergy 2020+ and the Technical University of Vienna, an industrial-sized dual fluidized bed biomass gasification system was simulated with Barracuda Virtual Reactor and compared with plant data.
Surface erosion is dependent upon many factors including surface material, particle material, particle shape, quality of surface installation, time in service, temperature, chemistry and certainly much more. A comprehensive model…
The use of a K-factor adjustment results in an additional pressure drop across a pressure Boundary Condition (BC) as a function of fluid flow. Using a non-zero K-factor value can…
Fluidized bed design and scale-up depends strongly on particle characteristics such as size and shape. Preliminary work on particle shear in a packed and fluidized beds, suggest that particle clustering can be measured and may provide a quantifiable metric for the level of particle clustering.
The CPFD methodology used in Barracuda solves both the fluid transport equations and the particle transport equations. The viscous terms in the fluid momentum equation utilize a Newtonian formulation -…
Barracuda Virtual Reactor is used in conjunction with a coke combustion kinetic model to evaluate and optimize regenerator hydrodynamics in order to increase product yield.
Peter Blaser, CPFD Software’s VP of Operations, will be speaking at the 54th Society of Chemical Engineers, Japan (SCEJ) Autumn Meeting Luncheon Seminar on September 12th, 2023, in Fukuoaka, Japan, virtually.
In this paper, researchers from Inaeris and CPFD Software validated results from Barracuda Virtual Reactor simulations using cold-flow experiments of Catalytic Fast Pyrolysis (CFP) fluidized beds.
In this work by Liu, Cattolica, and Seiser from UCSD, a three-dimensional model was established to simulate the hydrodynamics of a dual fluidized-bed gasification system.