The Operational Performance of an Ultrafiltration Pilot Unit for the Treatment of Ultra-Concentrated Brines

The valorization of ultra-concentrated seawater brines, named bitterns, requires preliminary purification processes, such as membrane filtration, before they can be fully exploited. This study investigates the performance of an ultrafiltration pilot plant aimed at separating organic matter and large particles from real bitterns. An empirical model for the bittern viscosity was developed to better characterize the membrane. Distinct variations in permeability, fouling resistance and rejection coefficient were observed under operational pressures ranging from 2 to 4 bar. Working at low pressure (2 bar), the pilot plant achieves permeability and rejection coefficient values of 17 L/m<sup>2</sup>hbar and 95%, respectively. Foulant behavior was characterized by determining a "fouling resistance", obtaining an average value of 1013 m<sup>-1</sup>. Tests with three distinct bittern samples were conducted to assess the influence of chemical composition and organic matter content on membrane permeability and fouling characteristics. The collected data enabled a comprehensive characterization of the ultrafiltration pilot unit working with this particular saline feed solution, which has very high technical-economic potential.

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Publication Details

Journal
Membranes
Published
2024-12-20
DOI
https://doi.org/10.3390/membranes14120276
Citations
1
Primary Topic
Membrane Separation Technologies
Type
article
Field-Weighted Citation Impact
0.20

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The Operational Performance of an Ultrafiltration Pilot Unit for the Treatment of Ultra-Concentrated Brines

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article

The Operational Performance of an Ultrafiltration Pilot Unit for the Treatment of Ultra-Concentrated Brines

I. Oller, Andrea Cipollina, Giuseppe Scelfo, Alessandro Tamburini, Fabrizio Vicari, Giorgio Micale, Ritamaria Raffaelli, Paula Serrano-Tari
article en
1 citations

Abstract

The valorization of ultra-concentrated seawater brines, named bitterns, requires preliminary purification processes, such as membrane filtration, before they can be fully exploited. This study investigates the performance of an ultrafiltration pilot plant aimed at separating organic matter and large particles from real bitterns. An empirical model for the bittern viscosity was developed to better characterize the membrane. Distinct variations in permeability, fouling resistance and rejection coefficient were observed under operational pressures ranging from 2 to 4 bar. Working at low pressure (2 bar), the pilot plant achieves permeability and rejection coefficient values of 17 L/m<sup>2</sup>hbar and 95%, respectively. Foulant behavior was characterized by determining a "fouling resistance", obtaining an average value of 1013 m<sup>-1</sup>. Tests with three distinct bittern samples were conducted to assess the influence of chemical composition and organic matter content on membrane permeability and fouling characteristics. The collected data enabled a comprehensive characterization of the ultrafiltration pilot unit working with this particular saline feed solution, which has very high technical-economic potential.

MembranesVol. 14(12)
Centro de Investigación y Desarrollo (ES), Centro de Investigaciones Energéticas, Medioambientales y Tecnológicas (ES), University of Almería (ES), University of Palermo (IT)
European Commission
Life below water
Openalex Percentile: Top 43%
Membrane Separation Technologies
0.20
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