2013
DOI: 10.1007/s13762-013-0284-2
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Zero-valent iron/persulfate(Fe0/PS) oxidation acetaminophen in water

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Cited by 95 publications
(32 citation statements)
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“…In order to solve this disadvantage, the use of ZVI has been proposed in literature, as an alternative to the addition of Fe 2+ given that ZVI allows a slow release of Fe 2+ to the aqueous phase, minimizing the extension of reaction. Studies with PS + ZVI concern mainly water treatment (Deng et al, 2014;Liang and Guo, 2010;Liang and Lai, 2008;Oh et al, 2009) and to a lower extent soil treatment (Oh and Shin, 2014), where a ZVI powder was used as activator of persulfate for the treatment of a diesel-contaminated soil. To solve the suitability of the injection of ZVI in geological porous the use of ZVI in the form of nanoparticles has been studied (Al-Shamsi and Thomson, 2013).…”
Section: Introductionmentioning
confidence: 99%
“…In order to solve this disadvantage, the use of ZVI has been proposed in literature, as an alternative to the addition of Fe 2+ given that ZVI allows a slow release of Fe 2+ to the aqueous phase, minimizing the extension of reaction. Studies with PS + ZVI concern mainly water treatment (Deng et al, 2014;Liang and Guo, 2010;Liang and Lai, 2008;Oh et al, 2009) and to a lower extent soil treatment (Oh and Shin, 2014), where a ZVI powder was used as activator of persulfate for the treatment of a diesel-contaminated soil. To solve the suitability of the injection of ZVI in geological porous the use of ZVI in the form of nanoparticles has been studied (Al-Shamsi and Thomson, 2013).…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, the development of new efficient approaches is required to decrease the TC antibiotic discharge into the environment. In general, advanced oxidation processes (AOPs) are the most efficient technology for degradation of various refractory pollutants in aqueous solutions and, during the last few decades, have been widely applied for removal of many organic pollutants such as ozonation (Khan et al 2010), Fenton (Zgajnar Gotvajn et al 2013), photo-Fenton (Liu et al 2012), ultrasound waves (Mahvi 2009;Mahvi et al 2009), sonochemical (Ifelebuegu et al 2014), photosonochemical processes (Mahvi and Maleki 2010;Hoseini et al 2013b), ultraviolet irradiation (Dobaradaran et al 2010), and sulfate radical-based oxidation (Tay et al 2013;Lin et al 2014;Deng et al 2014). In recent years, AOPs have been demonstrated to be an effective technology for the removal of pharmaceuticals, including TC antibiotics (Maroga et al 2012).…”
Section: Introductionmentioning
confidence: 99%
“…Two different types of fly ash (FA1 and FA2) have been reported as useful activators for treatment of pharmaceutical effluent, which decreased the activation energy from 122.56 kJ mol −1 to 23.32 and 47.64 kJ mol −1 , respectively [20]. In other research, the presence of Fe 0 as an activator to degrade acetaminophen resulted in the reduction of the activation energy from 120.4 to 36.1 kJ mol −1 [41]. The ESR at different temperatures ranging from 5 to 50 °C are presented in Table 1.…”
Section: Effect Of Temperature and Activation Energymentioning
confidence: 91%
“…However, as the CS/PS ratio was increased to 8, a slight growth in the removal efficiencies of COD and NH 3 was achieved, which may be due to the fact that the excessive amount of PS can react with SO4 •− , according to Equation (6) and convert it to sulfate ion [40]. Alternatively, sulfate radicals can react with each other; as a consequence, they have a quenching effect on the sulfate radical production at high concentration, according to Equation (7) [41]. Therefore, the PS/COD ratio of 4 was selected to perform the following experiments.…”
Section: Effect Of Converter Sludge Dosage and Ps/cod Mass Ratiomentioning
confidence: 99%