Reverse osmosis concentrate (ROC) produced as the by-product of the reverse osmosis process consists of a high load of organics (macro and micro) that potentially cause eco-toxicological effects in the environment. Previous studies focused on the removal of such compounds using oxidation, adsorption, and membrane-based treatments. However, these methods were not always efficient and formed toxic by-products. The impact of ion-exchange resin (IEX) (PuroliteA502PS) was studied in a micro-filtration-IEX hybrid system to remove organics from ROC for varying doses of Purolite A502PS (5-20 g/L) at a flux of 36 L/mh. The purolite particles in the membrane reactor reduced membrane fouling, evidenced by the reduction of transmembrane pressure (TMP), by pre-adsorbing the organics, and by mechanically scouring the membrane. The dissolved organic carbon was reduced by 45-60%, out of which 48-81% of the hydrophilics were removed followed by the hydrophobics and low molecular weight compounds (LMWs). This was based on fluorescence excitation-emission matrix and liquid chromatography-organic carbon detection. Negatively charged and hydrophobic organic compounds were preferentially removed by resin. Long-term experiments with different daily replacements of resin are suggested to minimize the resin requirements and energy consumption.
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http://dx.doi.org/10.3390/membranes13020136 | DOI Listing |
Water Res
January 2025
Kurita Water Industries Ltd., Nakano-ku, Tokyo 164-0001, Japan.
In the integrated circuit manufacturing process, reverse osmosis (RO) membranes are widely used for wastewater reclamation. However, fouling by typical surfactants significantly reduces membrane efficiency and lifespan. This study investigates the fouling mechanisms of typical surfactants-cetyl trimethyl ammonium bromide (CTAB, cationic), sodium dodecyl sulfate (SDS, anionic), and polyoxyethylene octyl phenyl ether (TX, nonionic)-on RO membranes.
View Article and Find Full Text PDFWater Res
January 2025
Department of Chemical and Biomolecular Engineering, Yonsei University, 50, Yonsei-ro, Seodaemun-gu, Seoul, 03722, Republic of Korea. Electronic address:
Seawater reverse osmosis (SWRO)-pressure retarded osmosis (PRO) hybrid desalination system is being actively researched to reduce energy consumption by generating energy in the PRO. However, the SWRO-PRO hybrid system still faces the following challenges: low freshwater recovery and low energy generation. To resolve these challenges, this study first proposes a novel SWRO-Solar-driven desalination (SD)-PRO hybrid system for energy-efficient desalination.
View Article and Find Full Text PDFMaterials (Basel)
December 2024
Department of Biotechnology and Bioprocess Engineering, Faculty of Chemical and Process Engineering, Warsaw University of Technology, Waryńskiego 1, 00-645 Warsaw, Poland.
Cleaning of surfaces without complex cleaning agents is an important subject, especially in food, pharmaceutical, and biomedical applications. The subject of microbubble and nanobubble cleaning is considered one of the most promising ways to intensify this process. In this work, we check whether and how the purity of water used for microbubble generation, as well as the gas used, affects the effectiveness of cleaning stainless-steel surfaces.
View Article and Find Full Text PDFNat Commun
January 2025
Department of Chemical and Biomolecular Engineering, National University of Singapore, Singapore, Republic of Singapore.
Employing electrochemistry for the selective functionalization of liquid alkanes allows for sustainable and efficient production of high-value chemicals. However, the large potentials required for C(sp)-H bond functionalization and low water solubility of such alkanes make it challenging. Here we discover that a Pt/IrO electrocatalyst with optimized Cl binding energy enables selective generation of Cl free radicals for C-H chlorination of alkanes.
View Article and Find Full Text PDFJ Environ Manage
December 2024
Air Liquide, Brussels, Belgium. Electronic address:
The operation of a reverse osmosis (RO) system is often severely hindered by the deposition of inorganic scales such as calcium carbonate on the membrane surface. Mitigation of this scaling phenomenon requires suitable pH control strategies, with the use of strong mineral acids (e.g.
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