dc.contributor.author |
Theologos, KM |
en |
dc.contributor.author |
Maroulis, ZB |
en |
dc.contributor.author |
Markatos, NC |
en |
dc.date.accessioned |
2014-03-01T01:13:24Z |
|
dc.date.available |
2014-03-01T01:13:24Z |
|
dc.date.issued |
1997 |
en |
dc.identifier.issn |
0737-3937 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/12444 |
|
dc.subject |
Computational fluid dynamics |
en |
dc.subject |
Drying |
en |
dc.subject |
Fluidization |
en |
dc.subject |
Modelling |
en |
dc.subject |
Numerical methods |
en |
dc.subject |
Simulation |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.classification |
Engineering, Mechanical |
en |
dc.subject.other |
FLOWS |
en |
dc.subject.other |
HEAT |
en |
dc.subject.other |
MASS |
en |
dc.title |
Simulation of transport dynamics in fluidized-bed dryers |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1080/07373939708917295 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1080/07373939708917295 |
en |
heal.language |
English |
en |
heal.publicationDate |
1997 |
en |
heal.abstract |
A mathematical model for predicting three-dimensional, two-phase flow, heat and mass transfer inside fluidized-bed dryers has been developed. The model consists of the full set of partial-differential equations that describe the conservation of mass, momentum and energy for both phases inside the dryer, and is coupled with correlations concerning interphase momentum-, heat-, and mass-transfer. It is shown that the model can predict. the most important engineering aspects of a fluidized-bed dryer including pressure drop, particle holdup, temperature distribution in both phases as well as drying efficiency all over the fluidized-bed. Plug-flow conditions are predicted for the gas phase, while back-mixing is predicted for the particles. The effect of particle mass-flow-rate on fluidized-bed dryer performance is evaluated. It is shown that the lower the particle mass flow-fate, the more intense the horizontal moisture gradients, while the higher the particle rate the more uniform the moisture distribution throughout the bed. |
en |
heal.publisher |
MARCEL DEKKER INC |
en |
heal.journalName |
Drying Technology |
en |
dc.identifier.doi |
10.1080/07373939708917295 |
en |
dc.identifier.isi |
ISI:A1997XC58100001 |
en |
dc.identifier.volume |
15 |
en |
dc.identifier.issue |
5 |
en |
dc.identifier.spage |
1265 |
en |
dc.identifier.epage |
1291 |
en |