Effect of functional groups of humic substances on uf performance
| Autor: | Oliver J. Hao, Shih-Hsiang Liu, Cheng-Fang Lin |
|---|---|
| Rok vydání: | 2001 |
| Předmět: |
Powdered activated carbon treatment
Environmental Engineering Ultrafiltration Chemical Fractionation Membrane technology Adsorption Phenols Water Supply Spectroscopy Fourier Transform Infrared Humic acid Waste Management and Disposal Humic Substances Water Science and Technology Civil and Structural Engineering chemistry.chemical_classification Chromatography Ecological Modeling Membrane fouling Titrimetry Membranes Artificial Carbon Dioxide Hydrogen-Ion Concentration Pollution Membrane Models Chemical chemistry Charcoal Titration Ion Exchange Resins Trihalomethanes |
| Zdroj: | Water Research. 35:2395-2402 |
| ISSN: | 0043-1354 |
| Popis: | The role of different functional groups present in humic substances on the membrane flux is unclear. This study is undertaken to (1) separate the carboxyl and phenolic groups from a humic solution, and (2) evaluate the effect of each fractionated humic substances on the ultrafiltration (UF) performance. A weak-base amine resin was used for the adsorption (pH 7) and the subsequent desorption (pH 13) of the phenolic groups from a commercial humic solution. These fractions were evaluated qualitatively (via Fourier transform infrared spectroscopy) and quantitatively (titration); they were further subjected to the analyses of the trihalomethane formation potential (THMFP) and ultrafiltration performance. Although, a complete separation of the phenolic and carboxyl groups is not possible, the results nevertheless provide useful information about their effects on UF performance. The fraction with a higher content of the phenolic OH group exhibits the highest THMFP (190 microg/mg C), whereas the fraction with a higher content of the carboxyl groups exhibits more flux decline. The UF system evaluated is unable to remove a significant portion of THM precursors, resulting in high THMs in permeate. The use of powdered activated carbon for the pretreatment of these fractions fails to improve membrane fouling. The pore size of UF membrane does not appear to affect the membrane flux, and the switch from the hydrophobic to hydrophilic membrane only slight improves the permeate flux. |
| Databáze: | OpenAIRE |
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