2010
DOI: 10.1590/s0100-40422010000500015
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Degradação eletroquímica do cloranfenicol em reator de fluxo

Abstract: Recebido em 19/8/09; aceito em 18/1/10; publicado na web em 23/4/10 ELECTROCHEMICAL DEGRADATION OF THE CHLORAMPHENICOL AT FLOW REACTOR. This paper reports a study of electrochemical degradation of the chloramphenicol antibiotic in aqueous medium using a flow-by reactor with DSA ® anode. The process efficiency was monitored by chloramphenicol concentration analysis with liquid chromatography (HPLC) during the experiments. Analysis of Total Organic Carbon (TOC) was performed to estimate the degradation degree an… Show more

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Cited by 16 publications
(10 citation statements)
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References 14 publications
(18 reference statements)
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“…The limitation imposed by mass transport is intensified by the low flow rate applied when the reactor is operated in the continuous flow mode, since this imposes a laminar flow inside the reactor and in the UV lamp compartment [34]. Under these conditions, increasing the flow rate promotes an increase in the internal velocity and consequently a decrease in internal retention time [50]. In the present study, increasing the flow rate in experiments performed in the absence of H 2 O 2 promoted a decrease in levofloxacin removal which, for anodic degradation, fell from 78.00 ± 0.09% at 300 mL h −1 to 63.00 ± 0.08 and 45% at 600 and 1200 mL h −1 , respectively.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…The limitation imposed by mass transport is intensified by the low flow rate applied when the reactor is operated in the continuous flow mode, since this imposes a laminar flow inside the reactor and in the UV lamp compartment [34]. Under these conditions, increasing the flow rate promotes an increase in the internal velocity and consequently a decrease in internal retention time [50]. In the present study, increasing the flow rate in experiments performed in the absence of H 2 O 2 promoted a decrease in levofloxacin removal which, for anodic degradation, fell from 78.00 ± 0.09% at 300 mL h −1 to 63.00 ± 0.08 and 45% at 600 and 1200 mL h −1 , respectively.…”
Section: Resultsmentioning
confidence: 99%
“…4). The poor removal of organic carbon may be associated with mass transport limitation to the anode surface and/or on the incidence of UV irradiation [50]. Much higher values for TOC removal were recorded in experiments with H 2 O 2 generation (GDE pressurized with O 2 ), and maximum removal of 86.00 ± 0.29% was attained under photo-Fenton conditions in which two separate processes were extant for the formation of hydroxyl radicals.…”
Section: Resultsmentioning
confidence: 99%
“…Such low levels of drug removal are also associated with small current densities under experimental conditions that promote degradation by the electrochemical process alone. 17 In contrast, experiments involving the generation of H 2 O 2 in the absence or presence of FeSO 4 .7H 2 O achieved reductions of 96% in the concentration of DIP at an applied potential −0.9 V (vs. Ag/AgCl). While both of these procedures were able to remove the analyte almost completely, the rate of degradation was greater under e-Fenton conditions.…”
Section: Resultsmentioning
confidence: 98%
“…Os mecanismos de oxidação dos compostos orgânicos poderão ser influenciados não só por reações a partir da geração dos radicais hidroxilas (COMNINELLIS, 1994), mas também pela presença de outras espécies oxidantes contidas no efluente. Como as AP apresentam quantidades consideráveis de íons cloreto (Cl -) provenientes dos sais dissolvidos nesse efluente, durante as eletrólises estes íons podem ser convertidos a espécies de cloro (Cl 2 ), que poderão reagir rapidamente com a água formando o ácido hipocloroso e/ou hipoclorito dependendo do pH do meio (pKa 7,53), que por sua vez auxiliam no processo de degradação da matéria orgânica (REZENDE et al, 2010).…”
Section: Introductionunclassified