Elsevier

Electrochimica Acta

Volume 181, 1 November 2015, Pages 200-207
Electrochimica Acta

ELECTRODIALYTIC PROCESS OF NANOFILTRATION CONCENTRATES – PHOSPHORUS RECOVERY AND MICROCYSTINS REMOVAL

https://doi.org/10.1016/j.electacta.2015.04.081Get rights and content

Abstract

Toxic cyanobacteria blooms are associated with nutrient enrichment of surface waters. Nanofiltration (NF) is a pressure-driven process that can be used in water treatment plants, to effectively remove particulate matter and organic contaminants, including cyanobacteria toxins, and nutrients. NF produces a nutrient and toxin-enriched stream, e.g. with microcystin-LR (MC-LR), that has to be safely disposed of.

The suitability of the electrodialytic (ED) process for phosphorus recovery and decrease of MC-LR concentrations from NF waste stream was assessed. In ED experiments running between 5 and 12 h, phosphorus electromigrated towards the anode compartment promoting an isolated clean phosphorus product. The maximum obtained phosphorus recovery was 84%, varying with the NF waste stream (membrane concentrate) characteristics, cell design and treatment time. After the application of the ED process the concentration of MC-LR was also reduced. These results encourage further tests, aiming the inclusion of this hybrid technology (NF followed by ED) in water treatment plants, contributing not only for the phosphorus recovery, but also for the decrease in the toxicity of the NF concentrate, lowering the costs and promoting safe disposal.

Section snippets

INTRODUCTION

The increase fluxes of nutrients arriving to water bodies, namely phosphorus and nitrogen, due to agricultural runoff/sewage treatment plants/other anthropogenic sources is one of the main factors to promote the existence of cyanobacterial blooms [1].

Microcystins are hepatotoxic cyclic peptide toxins (Fig. 1) released by freshwater cyanobacteria. Microcystin-LR (MC-LR) is the most common and toxic variant [2]. The contamination in freshwater sources may have severe health effects, leading the

Production of membrane concentrates

The production of membrane concentrate was carried out using a plate-and-frame unit (Lab-unit M20) described in detail elsewhere [10]. A thin film composite NF membrane with an hydraulic permeability of 82.2 kg/(h.m2.bar) at 21 °C and a membrane molecular weight cut-off of ca. 114 Da, NF90 (DowFilmtec), was used. The experiments consisted of concentration runs, mimetizing industrial NF operation at different water recovery rates (defined between permeate and initial feed volumes).

The concentrate

Phosphorus separation from membrane concentrates

Experiments A and B were carried out with the same membrane concentrate (#4; 1476 μS/cm) but different applied currents which led to different durations (7 and 5 h, respectively). Experiment C (10 mA; #5; 1276 μS/cm) had a similar duration as experiment A due to similar characteristics between the membrane concentrates used. Experiments A to C were considered finished when voltage started to be more constant, whereas Experiment D continued for 2 more hours to search for additional phosphorus

CONCLUSIONS

The suitability of the ED process to recover phosphorus and decrease of MC-LR concentrations from NF concentrate was assessed.

The electromigration of phosphorus towards the anode compartment resulted in recoveries between 32% and 84%, which were mainly dependent on membrane concentrate characteristics, cell design and time of the ED process. The behaviour of phosphorus migration may help a cost-benefit analysis of the best time needed to perform the nutrient recovery.

In the tested conditions,

ACKNOWLEDGEMENTS

Financial support for the work was provided by projects FP7-PEOPLE-2010-IRSES-269289-ELECTROACROSS - Electrokinetics across disciplines and continents: an integrated approach to finding new strategies for sustainable development and PTDC/ECM/111860/2009 - Electrokinetic treatment of sewage sludge and membrane concentrate: Phosphorus recovery and dewatering. Authors also thank RIARTAS-Red Iberoamericana de Aprovechamiento de Residuos Industriales para el Tratamiento de Suelos y Aguas

References (24)

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