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231225s2023 xx |||||o 00| ||eng c |
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|a 10.1080/09593330.2021.2012270
|2 doi
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|a pubmed24n1112.xml
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|a (DE-627)NLM333791606
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|a (NLM)34842066
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|a DE-627
|b ger
|c DE-627
|e rakwb
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|a eng
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| 100 |
1 |
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|a Tonhela, Marquele Amorim
|e verfasserin
|4 aut
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|a Electrodegradation of cyclophosphamide in artificial urine by combined methods
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|c 2023
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|a Text
|b txt
|2 rdacontent
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|a ƒaComputermedien
|b c
|2 rdamedia
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|a ƒa Online-Ressource
|b cr
|2 rdacarrier
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|a Date Completed 01.05.2023
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|a Date Revised 01.05.2023
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|a published: Print-Electronic
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|a Citation Status MEDLINE
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|a The degradation of the chemotherapeutic drug cyclophosphamide in artificial urine was evaluated by Electrochemical Advanced Oxidation Processes (EAOP). The system consisted of an electrochemical flow reactor with a commercial DSA® electrode (nominal composition Ti / Ru0,3Ti0,7O2) and Ti-mesh cathode. In order to assess the best parameters, the effect of current density, time and flow rate were analyzed using an initial 23 factorial design. The chosen response variable was the energy efficiency to produce free chlorine species (HClO/ClO-). After obtaining the most significant factors, the Central Composite Design (CCD) was performed, where the optimum conditions were determined for the current density range (11.714 mA cm-2 and 66.57 mA cm-2), flow rate (31.33 mL min-1) and time range (19 and 37 min). Under an optimized condition, the efficiency of other combined methods (photo-assisted electrochemical, photochemical, sonoelectrochemical and photo-assisted sonoelectrochemical) was evaluated. The efficiency of degradation processes was determined by removal of Chemical Oxygen Demand (COD), creatinine and urea. Analysis by HPLC demonstrates that the cyclophosphamide was substantially removed during the treatment process of ∼77%. Based on these results, it can be observed that the coupling between electrochemical and photochemical processes is a promising alternative for the treatment of this effluent, as a marked reduction of organic matter is observed (63, 94% of creatinine, 29.62% of urea, 39.1% of TOC) and a low treatment cost ratio
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|a Journal Article
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|a Active chlorine species
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|a advanced electrochemical oxidative processes
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|a cyclophosphamide
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|a effluent
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|a emerging contaminants
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|a Creatinine
|2 NLM
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|a AYI8EX34EU
|2 NLM
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|a Water Pollutants, Chemical
|2 NLM
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|a Chlorine
|2 NLM
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7 |
|a 4R7X1O2820
|2 NLM
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|a Urea
|2 NLM
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| 650 |
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|a 8W8T17847W
|2 NLM
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| 700 |
1 |
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|a Almeida, Maria Emília Veloso
|e verfasserin
|4 aut
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| 700 |
1 |
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|a Granato Malpass, Ana Claudia
|e verfasserin
|4 aut
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| 700 |
1 |
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|a Motheo, Artur de Jesus
|e verfasserin
|4 aut
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| 700 |
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|a Malpass, Geoffroy Roger Pointer
|e verfasserin
|4 aut
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| 773 |
0 |
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|i Enthalten in
|t Environmental technology
|d 1993
|g 44(2023), 12 vom: 28. Mai, Seite 1782-1797
|w (DE-627)NLM098202545
|x 1479-487X
|7 nnns
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| 773 |
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|g volume:44
|g year:2023
|g number:12
|g day:28
|g month:05
|g pages:1782-1797
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|u http://dx.doi.org/10.1080/09593330.2021.2012270
|3 Volltext
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