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      Algae-laden water treatment with ultrafiltration: effects of moderate oxidation by Fe(ii)/permanganate on hydraulically irreversible fouling and deposition of iron and manganese oxides

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          Abstract

          Application of ultrafiltration (UF) in algae-laden water treatment is hindered by severe fouling and low retention of soluble organics.

          Abstract

          Application of ultrafiltration (UF) in algae-laden water treatment is hindered by severe fouling and low retention of soluble organics. In this study, moderate oxidation by Fe( ii)/permanganate was investigated as a pretreatment for algae-laden water before UF in comparison with permanganate oxidation alone and Fe( ii) coagulation alone. Filtration tests were performed to assess the impacts of moderate oxidation on fouling reversibility, fouling mechanisms and compositions of the fouling layers. The results showed that Fe( ii)/permanganate substantially alleviated the flux reduction by 65% and reduced reversible resistances by nearly 2 orders of magnitude, because the agglomerates formed by foulants and in situ formed iron and manganese oxides were larger in size than the algal cells, resulting in more porous fouling layers. The fouling mechanism shifted from the dual mechanism of successive pore blocking and cake filtration to single standard blocking over the whole duration investigated. However, irreversible fouling was aggravated by Fe( ii)/permanganate, because the cake filtration was weakened and the adhesion of EOM on the membrane was aggravated in the presence of in situ formed iron and manganese oxides. The iron and manganese oxides deposited in the external fouling layer rather than inside the membrane. The amounts of Fe and Mn in the fouling layer substantially increased by more than 4 times with Fe( ii)/permanganate than with permanganate or Fe( ii). Fe( ii)/permanganate increased the removal of EOM (67%) by UF, attributing the enhanced adsorption of EOM to both the membrane and the agglomerates.

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          Fluorescence excitation-emission matrix regional integration to quantify spectra for dissolved organic matter.

          Excitation-emission matrix (EEM) fluorescence spectroscopy has been widely used to characterize dissolved organic matter (DOM) in water and soil. However, interpreting the > 10,000 wavelength-dependent fluorescence intensity data points represented in EEMs has posed a significant challenge. Fluorescence regional integration, a quantitative technique that integrates the volume beneath an EEM, was developed to analyze EEMs. EEMs were delineated into five excitation-emission regions based on fluorescence of model compounds, DOM fractions, and marine waters or freshwaters. Volumetric integration under the EEM within each region, normalized to the projected excitation-emission area within that region and dissolved organic carbon concentration, resulted in a normalized region-specific EEM volume (phi(i,n)). Solid-state carbon nuclear magnetic resonance (13C NMR), Fourier transform infrared (FTIR) analysis, ultraviolet-visible absorption spectra, and EEMs were obtained for standard Suwannee River fulvic acid and 15 hydrophobic or hydrophilic acid, neutral, and base DOM fractions plus nonfractionated DOM from wastewater effluents and rivers in the southwestern United States. DOM fractions fluoresced in one or more EEM regions. The highest cumulative EEM volume (phi(T,n) = sigma phi(i,n)) was observed for hydrophobic neutral DOM fractions, followed by lower phi(T,n) values for hydrophobic acid, base, and hydrophilic acid DOM fractions, respectively. An extracted wastewater biomass DOM sample contained aromatic protein- and humic-like material and was characteristic of bacterial-soluble microbial products. Aromatic carbon and the presence of specific aromatic compounds (as indicated by solid-state 13C NMR and FTIR data) resulted in EEMs that aided in differentiating wastewater effluent DOM from drinking water DOM.
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            A Combined Pore Blockage and Cake Filtration Model for Protein Fouling during Microfiltration.

            Zydney, Ho (2000)
            Previous studies of protein fouling during microfiltration have shown significant discrepancies between filtrate flux data and predictions of the classical pore blockage, pore constriction, and cake filtration models. A new mathematical model was developed for the filtrate flux which accounts for initial fouling due to pore blockage and subsequent fouling due to the growth of a protein cake or deposit over these initially blocked regions. The model explicitly accounts for the inhomogeneity in the cake layer thickness over different regions of the membrane arising from the time-dependent blockage of the pore surface. The model was shown to be in excellent agreement with experimental data obtained during the stirred cell filtration of bovine serum albumin solutions through polycarbonate track-etched microfiltration membranes over the entire course of the filtration. The model provides a smooth transition from the pore blockage to cake filtration regimes, eliminating the need to use different mathematical formulations to describe these two phenomena. In addition, the model provides the first quantitative explanation for some of the unusual observations reported previously in investigations of protein microfiltration. The results provide important insights into the underlying mechanisms of protein fouling during microfiltration. Copyright 2000 Academic Press.
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              Rapid synthesis of Ag/AgCl@ZIF-8 as a highly efficient photocatalyst for degradation of acetaminophen under visible light

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                Author and article information

                Contributors
                Journal
                ESWRAR
                Environmental Science: Water Research & Technology
                Environ. Sci.: Water Res. Technol.
                Royal Society of Chemistry (RSC)
                2053-1400
                2053-1419
                January 6 2021
                2021
                : 7
                : 1
                : 122-133
                Affiliations
                [1 ]Key Laboratory for Water Quality and Conservation of the Pearl River Delta
                [2 ]Guangzhou University
                [3 ]Guangzhou
                [4 ]P.R. China
                [5 ]College of Civil Engineering
                [6 ]Fuzhou University
                [7 ]Fuzhou
                [8 ]China
                Article
                10.1039/D0EW00833H
                c4b2c394-9022-4705-8651-a4f10ec73789
                © 2021

                http://rsc.li/journals-terms-of-use

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