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Statements

Subject Item
n2:RIV%2F00216275%3A25310%2F06%3A00004478%21RIV08-MSM-25310___
rdf:type
n6:Vysledek skos:Concept
dcterms:description
This contribution deals with the study of hollow fiber membrane dead-end microfiltration combined with powdered activated carbon sorption used in removing of organic dyes from wastewater. Adsorption characteristics of model reactive dye OSTAZIN RED on powdered activated carbon were studied. Adsorption isotherms and rate constant were determined from which followed, that adsorption of this dye on activated carbon is favorable, however the time to reach an equilibrium is around 7 days. From hybrid separation process characteristics measurements resulted that the activated carbon does not foul this type of membrane and the permeate flux is recovered after membrane backflush. A simple mathematical model describing dynamic sorptive process in microfiltration system is presented and discussed. This contribution deals with the study of hollow fiber membrane dead-end microfiltration combined with powdered activated carbon sorption used in removing of organic dyes from wastewater. Adsorption characteristics of model reactive dye OSTAZIN RED on powdered activated carbon were studied. Adsorption isotherms and rate constant were determined from which followed, that adsorption of this dye on activated carbon is favorable, however the time to reach an equilibrium is around 7 days. From hybrid separation process characteristics measurements resulted that the activated carbon does not foul this type of membrane and the permeate flux is recovered after membrane backflush. A simple mathematical model describing dynamic sorptive process in microfiltration system is presented and discussed. Příspěvek se zabývá studiem mikrofiltrace s dutými vlákny kombinované se sorpcí organického barviva na aktivním uhlí. Byly stanoveny sorpční charakteristiky použitého barviva (Ostazin red). Z naměřených charakteristik separačního procesu vyplynulo, že aktivní uhlí nezanáší nevratně membránu a zpětný proplach je vysoce účinný při obnově intenzity toku permeátu.Dále byl navržen jednoduchý matematický model popisující chování procesu sorpce jako součásti mikrofiltračního systému.
dcterms:title
Combined Membrane Process at Waste Water Treatment Combined Membrane Process at Waste Water Treatment Úprava odpadních vod pomocí kombinovaného membránového procesu
skos:prefLabel
Combined Membrane Process at Waste Water Treatment Úprava odpadních vod pomocí kombinovaného membránového procesu Combined Membrane Process at Waste Water Treatment
skos:notation
RIV/00216275:25310/06:00004478!RIV08-MSM-25310___
n3:strany
362-367
n3:aktivita
n16:Z
n3:aktivity
Z(MSM0021627502)
n3:dodaniDat
n12:2008
n3:domaciTvurceVysledku
n15:1790870 n15:4412257 n15:3154483
n3:druhVysledku
n4:D
n3:duvernostUdaju
n13:S
n3:entitaPredkladatele
n8:predkladatel
n3:idSjednocenehoVysledku
469104
n3:idVysledku
RIV/00216275:25310/06:00004478
n3:jazykVysledku
n19:eng
n3:klicovaSlova
Membrane microfiltration; Waste water; Hollow fiber; Activated carbon
n3:klicoveSlovo
n9:Waste%20water n9:Activated%20carbon n9:Membrane%20microfiltration n9:Hollow%20fiber
n3:kontrolniKodProRIV
[C09A5485CF94]
n3:mistoVydani
Compiegne, France
n3:nazevZdroje
Proceedings of the 2nd European Conference on Filtration and Separation
n3:obor
n5:CI
n3:pocetDomacichTvurcuVysledku
3
n3:pocetTvurcuVysledku
4
n3:rokUplatneniVysledku
n12:2006
n3:tvurceVysledku
Cakl, Jiří Markvartová, Olga Doleček, Petr Jiránková, Hana
n3:zamer
n20:MSM0021627502
s:numberOfPages
6
n18:hasPublisher
Université de Technologie de Compiegne
n14:isbn
2-913923-25-9
n11:organizacniJednotka
25310