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contributor authorBruce I. Dvorak
contributor authorMary Kay Maher
date accessioned2017-05-08T21:26:06Z
date available2017-05-08T21:26:06Z
date copyrightFebruary 1999
date issued1999
identifier other%28asce%290733-9372%281999%29125%3A2%28161%29.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/51342
description abstractMany drinking water utilities may choose to use granular activated carbon (GAC) to remove disinfection by-product precursors from their water to comply with proposed U.S. Environmental Protection Agency rules. Activated carbon usage rates can be minimized by blending effluents from multiple parallel GAC columns. An important issue for the preliminary design of GAC systems is to select the best column size (empty-bed contact time) and number of parallel columns. This study provides an example of the trade-offs between the activated carbon usage rate and frequency of regeneration, for one water source. The variables examined included empty-bed contact time and the number of parallel columns. The following two important trends were observed that apply to all utilities that use GAC: (1) The most dramatic improvement in the activated carbon usage rate from blending effluent occurs when going from one to two parallel columns, whereas the incremental improvement for adding more than two parallel columns decreases rapidly; and (2) a significant disadvantage of utilizing a large number of parallel columns is the need for frequent GAC replacement.
publisherAmerican Society of Civil Engineers
titleGAC Contactor Design for NOM Removal: Implications of EBCT and Blending
typeJournal Paper
journal volume125
journal issue2
journal titleJournal of Environmental Engineering
identifier doi10.1061/(ASCE)0733-9372(1999)125:2(161)
treeJournal of Environmental Engineering:;1999:;Volume ( 125 ):;issue: 002
contenttypeFulltext


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