Operational performance and cost analysis of PAC/ceramic MF for drinking water production: Exploring treatment capacity as a new indicator for performance assessment and optimization

[Display omitted] •Treatment capacity was proposed as a new performance indicator for microfiltration.•Treatment capacity combines productivity and energy needs.•Microfiltration treatment capacity maintained or slightly increased for PAC/MF.•Non-clarified waters required in line-coagulation to minim...

Full description

Saved in:
Bibliographic Details
Published inSeparation and purification technology Vol. 255; p. 117443
Main Authors Campinas, Margarida, Viegas, Rui M.C., Silva, Catarina, Lucas, Helena, Rosa, Maria João
Format Journal Article
LanguageEnglish
Published Elsevier B.V 15.01.2021
Subjects
Online AccessGet full text

Cover

Loading…
More Information
Summary:[Display omitted] •Treatment capacity was proposed as a new performance indicator for microfiltration.•Treatment capacity combines productivity and energy needs.•Microfiltration treatment capacity maintained or slightly increased for PAC/MF.•Non-clarified waters required in line-coagulation to minimize membrane fouling.•PAC/MF estimated total cost is 0.07–0.11 €/m3 for producing 100,000 m3/d. A powdered activated carbon (PAC)/ceramic microfiltration (MF) pilot was operated (24/7) in a water treatment plant during 18 months, with water from different points of the treatment line (raw, ozonated with recirculated filter-backwash waters, ozonated/pre-coagulated, filtered), the testing including MF and PAC/MF. The optimization of PAC/MF operational performance, including PAC effect analysis and pretreatment required, and a cost analysis are herein presented. A new indicator was developed and explored for performance assessment and optimization, the treatment capacity (TCp), i.e. the design flowrate normalized to membrane area and intake pressure. As expected, a higher TCp was obtained with filtered water. Non-clarified waters required alum-coagulation pretreatment to minimize membrane fouling, and achieved similar TCp results among them. PAC addition (6–24 mg/L) did not promote membrane fouling and had no or a slight positive effect on TCp. TCp integrates all key aspects of process productivity and therefore constitutes a useful indicator to balance flux, energy consumption, backwash frequency and chemical cleaning frequency. The cost functions developed for PAC/MF yielded, for the best operating conditions found for the low-turbidity, low-dissolved organic content waters tested, a total cost of 0.07–0.11€/m3 for 100,000 m3/d, including investment and operation costs.
ISSN:1383-5866
1873-3794
DOI:10.1016/j.seppur.2020.117443