Ultrafiltration membranes for drinking-water production from low-quality surface water: A case study in Spain
Identificadores
URI: https://hdl.handle.net/10481/101092Metadata
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Rojas-Serrano, Fátima; Álvarez Arroyo, Rocío; Pérez Pérez, Jorge Ignacio; Plaza, Fidel; Garralón, Gloria; Gómez Nieto, Miguel ÁngelMateria
Economical feasibility Fouling Natural organic matter Transmembrane pressure Ultrafiltration
Date
2015Referencia bibliográfica
Rojas-Serrano, F., Álvarez-Arroyo, R., Pérez, J. I., Plaza, F., Garralón, G., Gómez, M. A. (2015). Ultrafiltration membranes for drinking-water production from low-quality surface water: A case study in Spain. Membrane Water Treatment, 6(1), 77-94. https://doi.org/10.12989/mwt.2015.6.1.077
Sponsorship
Spanish Ministry of Science and Innovation (CTM2010-18899-TECNO); CADAGUA S.A.Abstract
Ultrafiltration membranes have several advantages over conventional drinking-water treatment.
However, this technology presents major limitations, such as irreversible fouling and low removal of natural
organic matter. Fouling depends heavily on the raw-water quality as well as on the operating conditions of
the process, including flux, permeate recovery, pre-treatment, chemical cleaning, and backwashing. Starting
with the premise that the optimisation of operating variables can improve membrane performance, different
experiments were conducted in a pilot plant located in Granada (Spain). Several combinations of permeate
and backwashing flow rates, backwashing frequencies, and aeration flow rates were tested for low-quality
water coming from Genil River with the following results: the effluent quality did not depend on the
combination of operating conditions chosen; and the membrane was effective for the removal of
microorganisms, turbidity and suspended solids but the yields for the removal of dissolved organic carbon
were extremely low. In addition, the threshold transmembrane pressure (-0.7 bar) was reached within a few
hours and it was difficult to recover due to the low efficiency of the chemical cleanings. Moreover, greater
transmembrane pressure due to fouling also increased the energy consumption, and it was not possible to
lower it without compromising the permeate recovery. Finally, the intensification of aeration contributed
positively to lengthening the operation times but again raised energy consumption. In light of these findings,
the feasibility of ultrafiltration as a single treatment is questioned for low-quality influents.