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Statements

Subject Item
n2:RIV%2F00216275%3A25310%2F12%3A39895243%21RIV13-MSM-25310___
rdf:type
skos:Concept n13:Vysledek
dcterms:description
A transient mathematical model has been followed to study the displacement washing of pulp bed composed of porous, compressible and cylindrical shaped fibres. The flow pattern of wash liquid through the bed can be described by a dispersion flow model involving Peclet number and Biot number. The effect of porosity along with Peclet number and Biot number on the solution profile of exit solute concentration via breakthrough curves has been studied. Concentration of solute adsorbed on fibre surface and intrapore solute concentration are related by Langmuir adsorption isotherm. Displacement washing has been simulated using a laboratory washing cell. Five runs of experiments have been performed on pulp beds formed from unbeaten, unbleached kraft fibres to check the authenticity of theoretical results. Axial dispersion coefficient is found to be influenced by interstitial velocity as well as the bed consistency. Washing process is affected collectively by Peclet number, Biot number and bed porosity. A transient mathematical model has been followed to study the displacement washing of pulp bed composed of porous, compressible and cylindrical shaped fibres. The flow pattern of wash liquid through the bed can be described by a dispersion flow model involving Peclet number and Biot number. The effect of porosity along with Peclet number and Biot number on the solution profile of exit solute concentration via breakthrough curves has been studied. Concentration of solute adsorbed on fibre surface and intrapore solute concentration are related by Langmuir adsorption isotherm. Displacement washing has been simulated using a laboratory washing cell. Five runs of experiments have been performed on pulp beds formed from unbeaten, unbleached kraft fibres to check the authenticity of theoretical results. Axial dispersion coefficient is found to be influenced by interstitial velocity as well as the bed consistency. Washing process is affected collectively by Peclet number, Biot number and bed porosity.
dcterms:title
Verification of mathematical model for displacement washing of kraft pulp fibres Verification of mathematical model for displacement washing of kraft pulp fibres
skos:prefLabel
Verification of mathematical model for displacement washing of kraft pulp fibres Verification of mathematical model for displacement washing of kraft pulp fibres
skos:notation
RIV/00216275:25310/12:39895243!RIV13-MSM-25310___
n13:predkladatel
n18:orjk%3A25310
n5:aktivita
n8:Z n8:I
n5:aktivity
I, Z(MSM0021627501)
n5:cisloPeriodika
2
n5:dodaniDat
n7:2013
n5:domaciTvurceVysledku
n12:1389424
n5:druhVysledku
n19:J
n5:duvernostUdaju
n10:S
n5:entitaPredkladatele
n16:predkladatel
n5:idSjednocenehoVysledku
177280
n5:idVysledku
RIV/00216275:25310/12:39895243
n5:jazykVysledku
n17:eng
n5:klicovaSlova
Langmuir isotherm; kraft pulp fibre; displacement washing; bed porosity; axial dispersion coefficient
n5:klicoveSlovo
n6:Langmuir%20isotherm n6:bed%20porosity n6:axial%20dispersion%20coefficient n6:kraft%20pulp%20fibre n6:displacement%20washing
n5:kodStatuVydavatele
IN - Indická republika
n5:kontrolniKodProRIV
[D12C6C2721DE]
n5:nazevZdroje
Indian Journal of Chemical Technology
n5:obor
n9:JJ
n5:pocetDomacichTvurcuVysledku
1
n5:pocetTvurcuVysledku
2
n5:rokUplatneniVysledku
n7:2012
n5:svazekPeriodika
19
n5:tvurceVysledku
Potůček, František Arora, Shelly
n5:wos
000302841700009
n5:zamer
n15:MSM0021627501
s:issn
0971-457X
s:numberOfPages
9
n14:organizacniJednotka
25310