Article
Characterization of DOM as a function of MW by fluorescence EEM and HPLC-SEC using UVA, DOC, and fluorescence detection.
Civil and Environmental Engineering, University of Colorado, Boulder, CO 80309, USA.
Water Research (impact factor:
4.86).
11/2003;
37(17):4295-303.
DOI:10.1016/S0043-1354(03)00317-8
pp.4295-303
Source: PubMed
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Article: Humic acid as a fouling agent in filtration
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ABSTRACT: Humic acid is a degradation product of lignin, carbohydrate and protein. It is contained in soils and therefore it is often present in surface waters in small amounts, which vary with the seasons. Besides giving the waters a yellowish to brownish color, the humic acid can also cause fouling problems in filtration of surface waters. In the present study humic acid was studied in different types of filtration processes because it seemed to be a problem at many mill sites using humic acid containing process waters. Humic acid was studied as a model substance in pressure and membrane filtration at different low concentrations. In the pressure filtration experiments it was added to a copper concentrate, containing as much iron and sulfur as copper. In membrane filtration it was filtered together with iron chloride. Also means to measure humic acid were investigated. In pressure filtration either capillary disc filters made of aluminum and silica oxides or filters made of different types of woven cloth were used. In membrane filtration the experiments were made with organic nano- and ultrafiltration membranes and with inorganic ultrafiltration membranes. The experiments were made on the laboratory scale. The humic acid could be analyzed using SEM-EDAX methods or with UV/VIS spectrophotometric methods. The studies showed that humic acid was most harmful in capillary pressure filtration. Even at small concentrations the filter was blocked and the cake did not form properly when added to the ore concentrates to be filtered. The flux decreased greatly with an addition of 10 ppm, and the filter was almost completely blocked when 100 ppm were added. In pressure filtration using cloth the harmful effect was not as remarkable. In membrane filtration humic acid did not disturb filtration as much as in pressure filtration even though it was used together with iron chloride. The effect of humic acid was a bit larger in ultrafiltration than in nanofiltration. The reason for the fouling tendency of humic acid seems to be its binding tendency to multivalent salts. The capillary filters used in pressure filtration are positively charged containing Al and Si. The humic acid is either not charged or somewhat negatively charged and probably forms chelates with the metals. It can be seen as a gel-like layer on the filter, which disturbs the formation of the cake and blocks the pores of the filter.Desalination. -
Article: Humic acid fouling during microfiltration
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ABSTRACT: A major factor limiting the use of microfiltration for surface water treatment is membrane fouling by natural organic matter. The extent and mechanisms of humic acid fouling during microfiltration have been examined using stirred cell filtration experiments and scanning electron microscopy. The extent of fouling was strongly dependent on both the source and preparation of the humic acid solutions. The large flux decline observed during constant pressure microfiltration was caused by the formation of a humic acid deposit located on the upper surface of the membrane. Prefiltration of the humic acid solutions dramatically reduced the rate of fouling through the removal of large humic acid aggregates. The initial fouling in this system was determined almost entirely by the convective deposition of these large particles/aggregates on the membrane surface. This initial deposit accelerated the subsequent rate of humic acid fouling, possibly serving as a nucleation site for deposition of macromolecular humic acids.Journal of Membrane Science. -
Article: Characterization of clean and natural organic matter (NOM) fouled NF and UF membranes, and foulants characterization
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ABSTRACT: Contact angles, zeta potentials, and IR spectra of clean and NOM-fouled membranes were compared to demonstrate differences in hydrophobicity, surface charge, and functional groups, respectively. Contact angle increased and decreased for membranes fouled with hydrophobic and hydrophilic NOM, respectively. Zeta potential decreased negatively (less negative) for membranes fouled with both hydrophobic and hydrophilic NOM, suggesting that ionizable functional groups were coated with non-ionizable NOM components (possibly neutrals). The IR spectra reduced in absorbance intensity for NOM-fouled membranes, suggesting that aromatic groups were coated with non-aromatic or less aromatic NOM components. The results of XAD- fractionations of foulants (desorbed NOM with NaOH) showed that hydrophilic and hydrophobic NOM components were the major foulants for membranes fouled with hydrophilic and hydrophobic NOM-source waters, respectively.Desalination.
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Keywords
apparent molecular weight
Barr Lake surface water
DOC measurement
DOM fractions
fluorescence EEM
Fluorescence excitation-emission matrix
fluorescence measurement
fulvic-like substances
HPLC)-size exclusion chromatography
HPSEC on-line fluorescence system
Irvine Ranch ground water
multiple on-line detectors enables
optimize water/wastewater treatment facilities
performance liquid chromatography
polysaccharide-like/protein-like substances
protein-like substances
qualitative DOM properties
quantitative DOC measurement
rapid analytical methods
specific MW components