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contributor authorKaren D. Pickering
contributor authorMark R. Wiesner
date accessioned2017-05-08T21:10:36Z
date available2017-05-08T21:10:36Z
date copyrightSeptember 1993
date issued1993
identifier other%28asce%290733-9372%281993%29119%3A5%28772%29.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/41576
description abstractA model for capital and operating costs of low‐pressure membrane filtration is presented. The model is used to explore the impact of variables describing system operation and membrane characteristics on treatment costs as well as to compare the cost of treating raw waters of different qualities using nanofiltration (NF), ultrafiltration (UF), and microfiltration (MF). The cost of UF or MF to remove particles from raw waters of moderate to high turbidity and concentrations of dissolved organic carbon (DOC) is calculated to be approximately twice that required to treat low‐turbidity streams or ground waters. At small design capacities (2,000 m
publisherAmerican Society of Civil Engineers
titleCost Model for Low‐Pressure Membrane Filtration
typeJournal Paper
journal volume119
journal issue5
journal titleJournal of Environmental Engineering
identifier doi10.1061/(ASCE)0733-9372(1993)119:5(772)
treeJournal of Environmental Engineering:;1993:;Volume ( 119 ):;issue: 005
contenttypeFulltext


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