Ferrous persulfate
(Fe(II)/S2O8
2–) oxidation
has gained much attention due to its outstanding oxidizability
and high efficiency in upgrading waste activated sludge (WAS) dewaterability.
Even though the Fe(II)/S2O8
2– technique possesses a myriad of advantages, its potential could
be further magnified for future upscaling and real-world application
especially when coupled with other alternative chemicals. In this
study, the potential benefits of Fe(II)/S2O8
2– oxidation coupled with natural zeolite and poly(dimethyl
diallyl ammonium chloride) (PDADMAC) for enhancing WAS dewaterability
were investigated. The vacuum filtration test was used to evaluate
the dewatering effectiveness. Variations in different extracellular
polymeric substance (EPS) fractions, water distribution, functional
groups, and microstructures were identified to elucidate the underlying
dewatering principles and kinetics. The results demonstrated that
the combination of Fe(II)/S2O8
2– with zeolite and PDADMAC had a significant effect on enhancing WAS
dewaterability. The optimal conditions obtained were 2.25/1.8 mmol-Fe(II)/S2O8
2–/g-VS, 0.5 g-zeolites/g-VS,
and 0.3 g-PDADMAC/g-VS with up to 117 g-H2O/g-VS removal
(moisture content: 64.5%). Further analysis revealed the three-step
dewatering mechanisms: (i) the SO4·– generated by Fe(II)/S2O8
2– oxidation attacked the WAS flocs and cells, broke the bonds of O–H,
C–C, and OCNH– in high-molecular-weight
biopolymers, and decomposed them into micromolecule organics and even
inorganics, thus liberating EPS- and cell-bound water, (ii) the broken
WAS flocs were then reflocculated via adsorption bridging and charge
neutralization induced by PDADMAC, and (iii) during the subsequent
filtration, zeolites created channels/cavities for water release by
forming a multiple void skeletal lattice while alleviating the clogging
of filtration cloth. In addition, the cost-benefit analysis revealed
that the combined Fe(II)/S2O8
2–/zeolites/PDADMAC process represented much greater attractiveness
in saving cost and real implementations than the zerovalent iron/persulfate
and classical Fenton process.