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Snoeyink, Vernon L. Mariñas, Benito J. Campos, Carlos 2015-09-25T21:05:08Z 2015-09-25T21:05:08Z 10000-01-01 1999 1999 The results of this study showed that, for a given carbon dose, the application of carbon as a pulse input always yields lower adsorbate concentrations in the membrane permeate. Furthermore, application of the activated carbon to continuous-flow reactors installed upstream of the membranes, and the recirculation to a floc blanket reactor after backwash results in significantly lower carbon dose for a given adsorbate removal. Made available in DSpace on 2015-09-25T21:05:08Z (GMT). No. of bitstreams: 2 license.txt: 4848 bytes, checksum: 96035ab3f5e1c23cc7138a224ce498bd (MD5) 9944809.pdf: 9203181 bytes, checksum: d50b0cc8a82b10dfbaf45c94582d812d (MD5) Previous issue date: 1999 Embargo set by: Seth Robbins for item 84756 Lift date: Forever Reason: Restricted to the U of I community idenfinitely during batch ingest of legacy ETDs Restricted to the U of I community idenfinitely during batch ingest of legacy ETDs U of I Only 236 p. Thesis (Ph.D.)--University of Illinois at Urbana-Champaign, 1999. http://hdl.handle.net/2142/83475 (MiAaPQ)AAI9944809 eng Engineering, Civil Modeling Powdered Activated Carbon Performance in Membrane Filtration Systems text Civl and Environmental Engineering Civl and Environmental Engineering University of Illinois at Urbana-Champaign Dissertation Ph.D.