Composition and reversibility of fouling on low-pressure membranes in the filtration of coagulated water: insights into organic fractions behaviour

Abstract

The primary problem for the application of microfiltration (MF) and ultrafiltration (UF) membrane technology is membrane fouling. Such is the case that understanding membrane fouling has become one of the major factors driving MF and UF membrane technology forward. Nevertheless, identifying the constituents that most contribute to membrane fouling and quantifying how they are detached when backwashing (BW) and cleaning-in-place (CIP) are applied still remains a challenging task. The aim of the present study was to quantify membrane fouling development during filtration and membrane fouling detachment during BW and CIP in terms of membrane permeability changes and masses of inorganic and organic constituents accumulated on the membrane. The study was conducted using bench-scale MF and UF modules fed with coagulated and settled water coming from a drinking water treatment plant and operated under dead-end and cross-flow operation modes. The experiments consisted inconsecutive permeation (20 min) alternated with BW with permeate water (1.0 min) (periodically chemically assisted with NaClO and NaOH) and followed by a two-stage CIP consisting first in an oxidising and basic step (NaClO and NaOH) and second in an acidic step (citric acid). Feed, permeate, retentate (when present) and cleaning discharge streams were monitored for turbidity, total and dissolved organic carbon (TOC and DOC, respectively), UV₂₅₄ and inorganic ions (Al, Fe, P). DOC was fractionated by high-performance size exclusion chromatography to gain insight into the behaviour of the different organic fractions. Results showed that both MF and UF membranes successfully removed turbidity, Al and Fe, whereas UV₂₅₄ was moderately removed and TOC and DOC poorly removed, with removal percentages higher for UF than for MF. With regard to the organic fractions, the largest molecular weight compounds were moderately removed while the smallest organic fractions seemed to totally permeate through both membranes. The results also showed that foulants were poorly washed out from the membrane by BW, but better extracted by the two-stage CIP up to a complete detachment for some foulants.

Keywords:

• Backwashing
• Fouling reversibility
• Microfiltration
• Organic fractions
• Surface water treatment
• Ultrafiltration

Acknowledgements

The authors gratefully acknowledge all personnel at Sant Joan Despí DWTP for their support and assistance throughout the study and the financial support from ACC1Ó through the OPTIMECA project (RD08-2-0023).

Notes

Presented at CEST2015–14th International Conference on Environmental Science and Technology, Rhodes, Greece, 3–5 September 2015