Extended discrete element method: Difference between revisions

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| pages=5728–5770
}}</ref> during
a review on particulate flows modelled with the CCDM approach. It has seen a mayor development in last two decades and describes motion of the solid phase by the [[Discrete Element Method]] (DEM) on an individual particle scale and the remaining phases are treated by the [[Navier-Stokes]] equations. Thus, the method is recognized as an effective tool to investigate into the interaction between a particulate and fluid phase as reviewed by Yu and Xu<ref>{{cite journal
last two decades and describes motion of the solid phase by the [[Discrete Element
Method]] (DEM) on an individual particle scale and the remaining phases
are treated by the [[Navier-Stokes]] equations. Thus, the method is recognized as
an effective tool to investigate into the interaction between a particulate and
fluid phase as reviewed by Yu and Xu <ref>{{cite journal
| first1=B. H.
| last1=Xu
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| volume=62
| pages=28–44
}}</ref>. Based on the CCDM methodology the characteristics of spouted and fluidised beds are predicted by Gryczka et al.<ref>{{cite journal
predicted by Gryczka et al. <ref>{{cite journal
| first1=O.
| last1=Gryczka
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}}</ref>.
 
The theoretical foundation for the '''Extended Discrete Element Method (XDEM)''' was developed in 1999 by Peters<ref>{{cite journal
'''Extended Discrete Element Method (XDEM)''' was developed in 1999 by Peters <ref>{{cite journal
| first1=B.
| last1=Peters
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| volume=116
| pages=297-301
}}</ref>, who described incineration of a wooden moving bed on a forward acting grate <ref>{{cite journal
| first1=B.
| last1=Peters
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| volume=131
| pages=132–146
}}</ref>. The concept was later also employed by Sismsek et al. <ref>{{cite journal
| first1=E.
| last1=Simsek
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codes such as Star-CD of [[CD-adapco]], [[Ansys]] and [[AVL]]-Fire. Droplets of a spray are treated by a zero-dimensional approach
to account for heat and mass transfer to the fluid phase.
 
 
 
==Methodology==