2018
DOI: 10.1016/j.cej.2018.05.178
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Investigating the aerated VUV/PS process simultaneously generating hydroxyl and sulfate radicals for the oxidation of cyanide in aqueous solution and industrial wastewater

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Cited by 62 publications
(29 citation statements)
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“…The simultaneous, multi-pathway mediatedFQs degradation in UV/K 2 S 2 O 8 could contribute to the enhancement of the reaction rate.One interesting observation is the synergistic effect arising from the combination of chemical addition and VUV irradiation, which accounted for the fastest degradation rate of FQs. The k obs values of VUV/H 2 O 2 and VUV/K 2 S 2 O 8 for OFX and NOF were comparable to the k obs of CEX at the same condition (> 2.0 min −1 ), which can be attributed to the generation of abundant reactive radical species of • OH/SO 4 •− in the modified VUV processes(Moussavi et al, 2018a). The VUV/H 2 O 2 process was reported to allow better degradation of clofibric acid (over 99% removal efficiency) compared to that by either UV/H 2 O 2 or VUV alone…”
mentioning
confidence: 64%
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“…The simultaneous, multi-pathway mediatedFQs degradation in UV/K 2 S 2 O 8 could contribute to the enhancement of the reaction rate.One interesting observation is the synergistic effect arising from the combination of chemical addition and VUV irradiation, which accounted for the fastest degradation rate of FQs. The k obs values of VUV/H 2 O 2 and VUV/K 2 S 2 O 8 for OFX and NOF were comparable to the k obs of CEX at the same condition (> 2.0 min −1 ), which can be attributed to the generation of abundant reactive radical species of • OH/SO 4 •− in the modified VUV processes(Moussavi et al, 2018a). The VUV/H 2 O 2 process was reported to allow better degradation of clofibric acid (over 99% removal efficiency) compared to that by either UV/H 2 O 2 or VUV alone…”
mentioning
confidence: 64%
“…(Li et al, 2011). Recently, Moussavi et al (2018a) revealed the enhancement of degradation of cyanide in industrial wastewater when employing VUV/K 2 S 2 O 8 process, possibly due to the simultaneous production of reactive radical species in a short period of time.…”
Section: Degradation Of Ofx Nof and Cex By Uv-and Vuv Based Processesmentioning
confidence: 99%
“…Fig. 5 shows that by the addition of tert-butanol, as a most common • OH scavenger, the ACT degradation did not change considerably (Moussavi et al, 2018), while the addition of salicylic acid reduced the ACT degradation efficiency to 41.6%. This can be explained by the reaction rate constant which has been reported 1.7 × 10 9 M − 1 s − 1 for ACT reaction with • OH (Yang et al, 2009), while the reaction rate constants for the reaction of • OH with the tert-butanol, and salicylic acid have been reported 6 × 10 8 and 2.2 × 10 10 M − 1 s − 1 , respectively (Crittenden et al, 2012).…”
Section: Mechanism Of Act Degradation In Copmentioning
confidence: 99%
“…The second-order rate constant of CNwith Fe(VI) is about 605 M -1 $s -1 at pH 8.0 (Sharma et al, 1998). Although it is lower than those of CNwith O 3 , HClO, and H 2 O 2 (Gurol and Bremen, 1985;Kepa et al, 2008;Moussavi et al, 2018), combing the oxidation capability of Fe(VI) and the coagulation capability of iron (III) offers an efficient approach to eliminate the CN -complexed heavy metals from water. It was found that 91.23% of CN -(1.0 mM) can be oxidized and 98.96% of Cu 2+ (0.094 mM) can be removed in minutes when 2.0 mM Fe(VI) was adopted to deal with the industrial wastewater containing cyanide-complexed Cu 2+ (Seung-Mok and Diwakar, 2009).…”
Section: Heavy Metalsmentioning
confidence: 99%