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Statements

Subject Item
n2:RIV%2F67985858%3A_____%2F10%3A00341593%21RIV11-AV0-67985858
rdf:type
n7:Vysledek skos:Concept
dcterms:description
A plug flow model is presented for the oxidation of hazardous carbon monoxide into inert carbon dioxide taking place in the freeboard region above a freely bubbling fluidized reactor. The extent of the reaction in oxygen- and water vapor-bearing flue gas is described as a function of the fraction of solids ejected into the freeboard from the bed surface, the relative throughput, the gas density, and the global rate of reaction. Experimental measurements were conducted to determine the axial concentration profiles of carbon monoxide and other species throughout the freeboard. Steady-state measurements were carried out in an electrically heated reactor with an inner diameter of 9.36 cm above a gently fluidized bed of heat-resistant ceramsite particles in which a precursive liquid fuel (isopropanol) was burned. A plug flow model is presented for the oxidation of hazardous carbon monoxide into inert carbon dioxide taking place in the freeboard region above a freely bubbling fluidized reactor. The extent of the reaction in oxygen- and water vapor-bearing flue gas is described as a function of the fraction of solids ejected into the freeboard from the bed surface, the relative throughput, the gas density, and the global rate of reaction. Experimental measurements were conducted to determine the axial concentration profiles of carbon monoxide and other species throughout the freeboard. Steady-state measurements were carried out in an electrically heated reactor with an inner diameter of 9.36 cm above a gently fluidized bed of heat-resistant ceramsite particles in which a precursive liquid fuel (isopropanol) was burned.
dcterms:title
High-Temperature Reaction in the Freeboard Region above a Bubbling Fluidized Bed High-Temperature Reaction in the Freeboard Region above a Bubbling Fluidized Bed
skos:prefLabel
High-Temperature Reaction in the Freeboard Region above a Bubbling Fluidized Bed High-Temperature Reaction in the Freeboard Region above a Bubbling Fluidized Bed
skos:notation
RIV/67985858:_____/10:00341593!RIV11-AV0-67985858
n3:aktivita
n8:Z n8:P
n3:aktivity
P(IAA400720701), Z(AV0Z40720504)
n3:cisloPeriodika
6
n3:dodaniDat
n17:2011
n3:domaciTvurceVysledku
n6:1866834 n6:2553473 n6:3190862 n6:2423251
n3:druhVysledku
n15:J
n3:duvernostUdaju
n13:S
n3:entitaPredkladatele
n9:predkladatel
n3:idSjednocenehoVysledku
261613
n3:idVysledku
RIV/67985858:_____/10:00341593
n3:jazykVysledku
n16:eng
n3:klicovaSlova
fluidization; freeboard; performance
n3:klicoveSlovo
n4:fluidization n4:performance n4:freeboard
n3:kodStatuVydavatele
US - Spojené státy americké
n3:kontrolniKodProRIV
[44117C1861A4]
n3:nazevZdroje
Industrial and Engineering Chemistry Research
n3:obor
n18:CI
n3:pocetDomacichTvurcuVysledku
4
n3:pocetTvurcuVysledku
4
n3:projekt
n12:IAA400720701
n3:rokUplatneniVysledku
n17:2010
n3:svazekPeriodika
49
n3:tvurceVysledku
Pohořelý, Michael Trnka, Otakar Svoboda, Karel Hartman, Miloslav
n3:wos
000275379400017
n3:zamer
n11:AV0Z40720504
s:issn
0888-5885
s:numberOfPages
9