dc.contributor.author |
Hatzilyberis, KS |
en |
dc.contributor.author |
Androutsopoulos, GP |
en |
dc.date.accessioned |
2014-03-01T01:14:24Z |
|
dc.date.available |
2014-03-01T01:14:24Z |
|
dc.date.issued |
1999 |
en |
dc.identifier.issn |
0737-3937 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/13048 |
|
dc.subject |
Allothermal gasification plant |
en |
dc.subject |
Particle size segregation |
en |
dc.subject |
Residence time |
en |
dc.subject |
Rotary kiln |
en |
dc.subject |
Rotating drum |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.classification |
Engineering, Mechanical |
en |
dc.subject.other |
Dryers (equipment) |
en |
dc.subject.other |
Flow of solids |
en |
dc.subject.other |
Gasification |
en |
dc.subject.other |
Industrial plants |
en |
dc.subject.other |
Lignite |
en |
dc.subject.other |
Particles (particulate matter) |
en |
dc.subject.other |
Phase separation |
en |
dc.subject.other |
Rotary kilns |
en |
dc.subject.other |
Rotational flow |
en |
dc.subject.other |
Allothermal gasification plant |
en |
dc.subject.other |
Flighted drum case |
en |
dc.subject.other |
Particle size segregation |
en |
dc.subject.other |
Residence time distribution |
en |
dc.subject.other |
Rotating drum |
en |
dc.subject.other |
Tracer pulse input response experiments |
en |
dc.subject.other |
Mass transfer |
en |
dc.subject.other |
dryer |
en |
dc.subject.other |
flow |
en |
dc.subject.other |
gasification |
en |
dc.subject.other |
lignite processing |
en |
dc.subject.other |
particle size analysis |
en |
dc.subject.other |
residence time |
en |
dc.title |
An RTD study for the flow of lignite particles through a pilot rotary dryer. Part II: Flighted drum case |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1080/07373939908917568 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1080/07373939908917568 |
en |
heal.language |
English |
en |
heal.publicationDate |
1999 |
en |
heal.abstract |
In Part II of this work a flighted pilot rotating cylindrical drum, intended to be used as either a dryer or calciner (kiln), has been used to investigate the flow, through it, of pulverized moist lignite. Tracer pulse input - response experiments have been performed. Residence Time Distribution (RTD) data have been deduced for three types of flight geometry, namely: Rectangular (RA), Equal Angular Distribution (E.A.D.) and Equal Horizontal Distribution (E.H.D.). For each flight shape, mean residence time t̄ has been correlated with drum operating conditions. The sequence t̄(EAD) < t̄(RA) < t̄(EHD) has been validated. A comparison between the residence time predictions for the flighted and the bare drum has indicated that t̄ for the former may be higher by up to 3.5 times than that for the latter. Exceptionally high solids hold-up values (i.e., Z = 0.13 - 0.42) have been observed and compared to theoretical predictions. Particle size segregation during lignite flow through the flighted drum was not confirmed.In Part II of this work a flighted pilot rotating cylindrical drum, intended to be used as either a dryer of calciner (kiln), has been used to investigate the flow, through it, of pulverized moist lignite. Tracer pulse input - response experiments have been performed. Residence Time Distribution (RTD) data have been deduced for three types of flight geometry, namely: Rectangular (RA), Equal Angular Distribution (E.A.D.) and Equal Horizontal Distribution (E.H.D.). For each flight shape, mean residence time t̄ has been correlated with drum operating conditions. The sequence t̄EAD < t̄RA < t̄EHD has been validated. A comparison between the residence time predictions for the flighted and the bare drum has indicated that t̄ for the former may be higher by up to 3.5 times than that for the latter. Exceptionally high solids hold-up values (i.e., 2 = 0.13 - 0.42) have been observed and compared to theoretical predictions. Particle size segregation during lignite flow through the flighted drum was not confirmed. |
en |
heal.publisher |
Marcel Dekker Inc, New York, NY, United States |
en |
heal.journalName |
Drying Technology |
en |
dc.identifier.doi |
10.1080/07373939908917568 |
en |
dc.identifier.isi |
ISI:000080188000007 |
en |
dc.identifier.volume |
17 |
en |
dc.identifier.issue |
4-5 |
en |
dc.identifier.spage |
759 |
en |
dc.identifier.epage |
774 |
en |