Gas solid fluidized bed is the most common solid-gas contractors in many processes like reactions, drying, coating and size separation. The unique heat & mass transfer capabilities between phases and robust mixing make fluidized bed a good candidate for many gas-solid processing units. In practical applications, they can operate in bubbling, turbulent, and fast fluidization. A combination of fast fludization bed with a downer bed creates a new model for solid-gas contact, named circulating fluidized bed, in which multiple operation can be integrated into one processing unit.
Fludized beds can operate as a size/density solid classifier, a heterogeneous reactor (catalytic), a polymerization reactor, a combustion reactor, a adsorber unit for hydrocarbons (VOCs), a chemical looping combustion system, a dryer, a granulator, and a coater. All these processes contain complex phenomena that occur simultaneously. Therefore, design and scale up of these beds require a deep understanding of all these phenomena. The first necessary step, is to understand the hydrodynamics of a fluidized bed; though it is not enough for a complete analysis of these units.
In this video you see an animation of a gas-solid fluidized bed operating at bubbling regime. Particles are sand (2500 kg/m3) with mean diameter of 275 micron. Superficial air velocity at atmospheric pressure and 288 K is 0.38 m/s. The simulation has been performed using OpenFOAM® 7 and visualized using Paraview®.
if you cannot see the video properly, click here.
Respected sir,
I am writing in reference to the project entitled ” Computational Study of Agglomeration Mitigation in Fluidized Bed Combustor ” under the kind supervision of Prof. Dr. AttaUllah(PIEAS, Islamabad).
I have to mitigate Agglomeration problem using bed additives in FBCs and simulate it in ANSYS FLUENT which includes the coupling of Multiphase (Eulerian) , species transport (Reactions) , Population Balance Model(for Particle size distribution of agglomerates formed) , Solidification/Melting ( Ash Melting phenomena) . i.e CFD-PBM coupling.
Sir, I simulated the models separately but was unable to couple them simultaneously. If you can provide any path or steps to couple these models or any kind of help . I will be grateful to you.
I also explored different research articles in which authors used various commercial softwares like Barracuda, Mfix, Openfoam for similar kind of work. You can also give your valuable opinion either which approach or software i should use to account for coupling. Published experimental paper is attached for further clearance and understanding of the said topic
Looking forward to hearing from you.
Regards
Abdullah Tasleem
MS Process Engineering
PIEAS, Islamabad
WhatsApp: +923056760785
Email: mspe2015@pieas.edu.pk
Email:abdullahtasleem785@gmail.com
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