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contributor authorCarlos Campos
contributor authorBenito J. Mariñas
contributor authorVernon L. Snoeyink
contributor authorIsabelle Baudin
contributor authorJean Michel Lainé
date accessioned2017-05-08T21:28:54Z
date available2017-05-08T21:28:54Z
date copyrightFebruary 2000
date issued2000
identifier other%28asce%290733-9372%282000%29126%3A2%28104%29.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/53142
description abstractThe models developed in the first part of this study are applied to predict the removal of 4-nitrophenol by powdered activated carbon (PAC) in a bench-scale reactor. A series of continuous-flow filtration experiments were conducted with different carbon doses to verify the modeling approach when the activated carbon was added directly to the membrane reactor, either as step or pulse input, and when the carbon was dosed as a step input to a continuous-flow stirred tank reactor followed by the membrane reactor. The models predicted well the experimental data for all cases investigated. The verified model was used to investigate the effect of various operating parameters on the efficiency of the adsorption process. This analysis included the effect of filtration time, membrane reactor volume, dosing procedure, and the effect of dosing the carbon in reactors installed in series upstream of the membrane reactor.
publisherAmerican Society of Civil Engineers
titlePAC-Membrane Filtration Process. II: Model Application
typeJournal Paper
journal volume126
journal issue2
journal titleJournal of Environmental Engineering
identifier doi10.1061/(ASCE)0733-9372(2000)126:2(104)
treeJournal of Environmental Engineering:;2000:;Volume ( 126 ):;issue: 002
contenttypeFulltext


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