Control of dissolved organic matter fouling ultrafiltration membrane treating a WWTP secondary effluent via multi-pretreatments

Dissolved organic matter (DOM) has been regarded as a major organic foulant resulting in UF membrane fouling in wastewater reclamation. This study investigated the effects of multi-pretreatments, including coagulation, adsorption, and pre-oxidation, of a WWTP secondary effluent via adding Al-2(SO4)(3)/diatomite composite, FeCl3, GAC, and O-3 to control DOM fouling UF membrane. Results showed the membrane fluxes increased by 18.1, 8.1, 5.3, and 0.1% and membrane resistances decreased by 58.9, 28.9, 17.8, and 2.2%, when the optimal adding dosages of Al-2(SO4)(3)/diatomite composite, FeCl3, GAC, and O-3 were 400, 80, 80, and 6mgL(-1), respectively. The tests of a series of UF membranes with different pore sizes demonstrated that DOM of 10,000-30,000Dalton MW in the secondary effluent was dramatically reduced by adding Al-2(SO4)(3)/diatomite composite, FeCl3, and GAC. This fractionation was mainly protein-like substances characterized by 3DEEM fluorescence spectroscopy. Additionally, adding Al-2(SO4)(3)/diatomite composite was available for removing humic acid-like substances simultaneously. Although O-3 addition effectively oxidized protein-like and humic acid-like substances, it could induce the increase in DOM of <4,000Dalton MW up to 80.1% and triggered the UF membrane fouling. Combination of MW distribution, SEM and 3DEEM, the DOM fractionation of <6,000Dalton MW, mainly humic acid-like substances, easily caused UF membrane fouling. Consequently, compared with adsorption and pre-oxidation, the coagulation of Al-2(SO4)(3)/diatomite composite, the first time used for the pretreatment of DOM, was proved to be the best additive for controlling UF membrane fouling.