This HTML5 document contains 45 embedded RDF statements represented using HTML+Microdata notation.

The embedded RDF content will be recognized by any processor of HTML5 Microdata.

Namespace Prefixes

PrefixIRI
dctermshttp://purl.org/dc/terms/
n10http://linked.opendata.cz/resource/domain/vavai/vysledek/RIV%2F60461373%3A22340%2F10%3A00023528%21RIV11-MSM-22340___/
n3http://localhost/temp/predkladatel/
n8http://linked.opendata.cz/resource/domain/vavai/riv/tvurce/
n12http://linked.opendata.cz/ontology/domain/vavai/
n17http://linked.opendata.cz/resource/domain/vavai/zamer/
shttp://schema.org/
skoshttp://www.w3.org/2004/02/skos/core#
n4http://linked.opendata.cz/ontology/domain/vavai/riv/
n2http://linked.opendata.cz/resource/domain/vavai/vysledek/
rdfhttp://www.w3.org/1999/02/22-rdf-syntax-ns#
n5http://linked.opendata.cz/ontology/domain/vavai/riv/klicoveSlovo/
n11http://linked.opendata.cz/ontology/domain/vavai/riv/duvernostUdaju/
xsdhhttp://www.w3.org/2001/XMLSchema#
n18http://linked.opendata.cz/ontology/domain/vavai/riv/jazykVysledku/
n15http://linked.opendata.cz/ontology/domain/vavai/riv/aktivita/
n16http://linked.opendata.cz/ontology/domain/vavai/riv/obor/
n7http://linked.opendata.cz/ontology/domain/vavai/riv/druhVysledku/
n6http://reference.data.gov.uk/id/gregorian-year/

Statements

Subject Item
n2:RIV%2F60461373%3A22340%2F10%3A00023528%21RIV11-MSM-22340___
rdf:type
n12:Vysledek skos:Concept
dcterms:description
The axial dispersions of gas and liquid phase in a column of inner diameter 0.297 m packed with random packing of metal Pall rings 25 and Intalox saddles 25 and structured packing of Mellapak 250Y were measured using a dynamic method under hydraulic conditions common in distillation columns, i. e., liquid flow rate from 6.94?10-4 to 0.0111 m/s and gas flow rate from 0.25 to 2 m/s. The two response method with a diffusion-type model was used to reproduce the experimental response curves. Axial mixing in the gas increases with gas and liquid rates for both random and structured packings but the dependence on the gas rate is very weak for the structured packing. The largest gas mixing was found for the Pall rings at the highest gas rate, the least was found for the structured packing at the lowest gas and liquid rates. Liquid-phase axial mixing increases with decreasing liquid flow rate and is independent of gas flow rate for both random and structured packings. The largest liquid mixing was found for th The axial dispersions of gas and liquid phase in a column of inner diameter 0.297 m packed with random packing of metal Pall rings 25 and Intalox saddles 25 and structured packing of Mellapak 250Y were measured using a dynamic method under hydraulic conditions common in distillation columns, i. e., liquid flow rate from 6.94?10-4 to 0.0111 m/s and gas flow rate from 0.25 to 2 m/s. The two response method with a diffusion-type model was used to reproduce the experimental response curves. Axial mixing in the gas increases with gas and liquid rates for both random and structured packings but the dependence on the gas rate is very weak for the structured packing. The largest gas mixing was found for the Pall rings at the highest gas rate, the least was found for the structured packing at the lowest gas and liquid rates. Liquid-phase axial mixing increases with decreasing liquid flow rate and is independent of gas flow rate for both random and structured packings. The largest liquid mixing was found for th
dcterms:title
Gas and liquid axial mixing in the column packed with Mellakak 250Y, Pall rings and Intalox saddles 25 under flow conditions prevailing in dislillation columns Gas and liquid axial mixing in the column packed with Mellakak 250Y, Pall rings and Intalox saddles 25 under flow conditions prevailing in dislillation columns
skos:prefLabel
Gas and liquid axial mixing in the column packed with Mellakak 250Y, Pall rings and Intalox saddles 25 under flow conditions prevailing in dislillation columns Gas and liquid axial mixing in the column packed with Mellakak 250Y, Pall rings and Intalox saddles 25 under flow conditions prevailing in dislillation columns
skos:notation
RIV/60461373:22340/10:00023528!RIV11-MSM-22340___
n4:aktivita
n15:Z
n4:aktivity
Z(MSM6046137306)
n4:cisloPeriodika
1
n4:dodaniDat
n6:2011
n4:domaciTvurceVysledku
n8:8871213 n8:4819306 n8:7287615
n4:druhVysledku
n7:J
n4:duvernostUdaju
n11:S
n4:entitaPredkladatele
n10:predkladatel
n4:idSjednocenehoVysledku
260224
n4:idVysledku
RIV/60461373:22340/10:00023528
n4:jazykVysledku
n18:eng
n4:klicovaSlova
longitudinal mixing; axial dispersion; packed column; Mellapak 250Y; Pall rings 25; Intalox saddles 25
n4:klicoveSlovo
n5:Mellapak%20250Y n5:Intalox%20saddles%2025 n5:axial%20dispersion n5:Pall%20rings%2025 n5:packed%20column n5:longitudinal%20mixing
n4:kodStatuVydavatele
US - Spojené státy americké
n4:kontrolniKodProRIV
[4855E46A78EC]
n4:nazevZdroje
Ind.Eng.Chem., Res.
n4:obor
n16:CI
n4:pocetDomacichTvurcuVysledku
3
n4:pocetTvurcuVysledku
3
n4:rokUplatneniVysledku
n6:2010
n4:svazekPeriodika
49
n4:tvurceVysledku
Rejl, František Valenz, Lukáš Linek, Václav
n4:wos
000282727300050
n4:zamer
n17:MSM6046137306
s:issn
0888-5885
s:numberOfPages
11
n3:organizacniJednotka
22340