Integration of a 3D-printed electrochemical reactor with a tubular membrane photoreactor to promote sulfate-based advanced oxidation processes

• Integration of SERPIC-UCLM® cell and TMPr for phototreatment of RO C /NF C by SR-AOPs. • SERPIC-UCLM® cell presents enhanced mass transport compared to existing reactors. • PMSA self-decomposes at neutral pH of RO C /NF C into PMS. • PMS and PDS showed the same degradation patterns of CECs in RO C /NF C phototreatment. • 2.4 mM PMS increased the CECs degradation and ensured compliance with regulations. This study investigates the integration of an in-house 3D printed electrochemical cell − SERPIC-UCLM® cell – for the in situ generation of peroxymonosulfuric acid (PMSA) with a lab-scale tubular membrane photoreactor (TMPr) to evaluate the effectiveness of sulfate-radical advanced oxidation processes (SR-AOPs) in eliminating contaminants of emerging concern (CECs) from reverse osmosis and nanofiltration concentrates (RO C and NF C , respectively). First, the SERPIC-UCLM® cell was evaluated in terms of mass transport features employing the limiting current technique, demonstrating favorable volumetric mass transport rates ( k m A ∼ 10 –3 s – 1 ) and Sherwood values ( Sh > 300) under the laminar flow regime (110 < Reynolds ( Re ) < 790). Afterward, the effect of the electrolyte (sulfuric acid, H 2 SO 4 ) initial pH in the electrochemical generation of PMSA was studied, with an initial pH of 1 selected as optimal. PMSA is a highly reactive peroxyacid that undergoes self-decomposition at neutral pH media (e.g., RO C and NF C with a pH of 7.6 and 7.9, respectively), primarily existing in the form of peroxomonosulfate (PMS). Additionally, the phototreatment of the RO C and NF C was assessed using the electrogenerated PMS and commercial peroxydisulfate (PDS) under the same conditions. The results indicated comparable degradation patterns for CECs in both RO C and NF C . Furthermore, the application of 2.4 mM PMS resulted in removals higher than 60 % for 7 of the 11 CECs identified in the NF C , and ensured compliance with wastewater discharge regulations for pH, chemical oxygen demand (COD), and total suspended solids (TSS) levels. These findings emphasize the importance of this technology, showing its advantages in terms of versatility and logistics.

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Publication Details

Journal
Chemical Engineering Journal
Published
2024-10-24
DOI
https://doi.org/10.1016/j.cej.2024.156900
Citations
7
Primary Topic
Advanced oxidation water treatment
Type
article
Field-Weighted Citation Impact
1.41

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article

Integration of a 3D-printed electrochemical reactor with a tubular membrane photoreactor to promote sulfate-based advanced oxidation processes

Lothar Schäfer, Jan Gäbler, Rosa Montes, Rosario Rodil et al.
7 citations
Chemical Engineering Journal
Advanced oxidation water treatment
1.41
article

Integration of a 3D-printed electrochemical reactor with a tubular membrane photoreactor to promote sulfate-based advanced oxidation processes

Lothar Schäfer, Jan Gäbler, Rosa Montes, Rosario Rodil, Ismael F. Mena, Miguel Montiel, Cristina Sáez, Vítor J.P. Vilar, Ana I. Gomes, Manuel A. Rodrigo, Francisca C. Moreira, José Benito Quintana, Carla S. Santos, Agustina R. de Olivera
article en
7 citations

Abstract

• Integration of SERPIC-UCLM® cell and TMPr for phototreatment of RO C /NF C by SR-AOPs. • SERPIC-UCLM® cell presents enhanced mass transport compared to existing reactors. • PMSA self-decomposes at neutral pH of RO C /NF C into PMS. • PMS and PDS showed the same degradation patterns of CECs in RO C /NF C phototreatment. • 2.4 mM PMS increased the CECs degradation and ensured compliance with regulations. This study investigates the integration of an in-house 3D printed electrochemical cell − SERPIC-UCLM® cell – for the in situ generation of peroxymonosulfuric acid (PMSA) with a lab-scale tubular membrane photoreactor (TMPr) to evaluate the effectiveness of sulfate-radical advanced oxidation processes (SR-AOPs) in eliminating contaminants of emerging concern (CECs) from reverse osmosis and nanofiltration concentrates (RO C and NF C , respectively). First, the SERPIC-UCLM® cell was evaluated in terms of mass transport features employing the limiting current technique, demonstrating favorable volumetric mass transport rates ( k m A ∼ 10 –3 s – 1 ) and Sherwood values ( Sh > 300) under the laminar flow regime (110 < Reynolds ( Re ) < 790). Afterward, the effect of the electrolyte (sulfuric acid, H 2 SO 4 ) initial pH in the electrochemical generation of PMSA was studied, with an initial pH of 1 selected as optimal. PMSA is a highly reactive peroxyacid that undergoes self-decomposition at neutral pH media (e.g., RO C and NF C with a pH of 7.6 and 7.9, respectively), primarily existing in the form of peroxomonosulfate (PMS). Additionally, the phototreatment of the RO C and NF C was assessed using the electrogenerated PMS and commercial peroxydisulfate (PDS) under the same conditions. The results indicated comparable degradation patterns for CECs in both RO C and NF C . Furthermore, the application of 2.4 mM PMS resulted in removals higher than 60 % for 7 of the 11 CECs identified in the NF C , and ensured compliance with wastewater discharge regulations for pH, chemical oxygen demand (COD), and total suspended solids (TSS) levels. These findings emphasize the importance of this technology, showing its advantages in terms of versatility and logistics.

Chemical Engineering JournalVol. 500
Universidade do Porto (PT), Universidade de Santiago de Compostela (ES), Fraunhofer Institute for Surface Engineering and Thin Films (DE), University of Castilla-La Mancha (ES)
Fundação para a Ciência e a Tecnologia
Clean water and sanitation
Openalex Percentile: Top 20%
Advanced oxidation water treatment
1.41
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