Batch and Continuous Photo-Fenton Oxidation of Reactive-Red Dye from Wastewater

This paper aimed to investigate the ability of photo-Fenton technology to remove Reactive Red dye (RR-‎dye) from wastewater using batch and continuous operating modes. The batch mode of photo-Fenton ‎removal of organic content was conducted under the influence of solution pH (3-10), hydrogen peroxid...

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Autores principales: Ali A. Hassan, Forat Yasir AlJaberi, Raid ‎ T. Al-Khateeb
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Lenguaje:EN
Publicado: Polish Society of Ecological Engineering (PTIE) 2022
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Acceso en línea:https://doaj.org/article/f51fae76be2541c0851c58abad4e408b
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spelling oai:doaj.org-article:f51fae76be2541c0851c58abad4e408b2021-12-01T13:20:42ZBatch and Continuous Photo-Fenton Oxidation of Reactive-Red Dye from Wastewater2299-899310.12911/22998993/143864https://doaj.org/article/f51fae76be2541c0851c58abad4e408b2022-01-01T00:00:00Zhttp://www.jeeng.net/Batch-and-Continuous-Photo-Fenton-Oxidation-of-Reactive-Red-Dye-from-Wastewater,143864,0,2.htmlhttps://doaj.org/toc/2299-8993This paper aimed to investigate the ability of photo-Fenton technology to remove Reactive Red dye (RR-‎dye) from wastewater using batch and continuous operating modes. The batch mode of photo-Fenton ‎removal of organic content was conducted under the influence of solution pH (3-10), hydrogen peroxide ‎‎(25-100 ppm), irradiation time (20-90 min), ferrous sulfate (5-20 ppm), and temperature (25-60oC). For ‎comparison, the continuous treatment was conducted under the influence of the flow rate of the ‎contaminated solution (10, 20, 30, 40, and 50 mL/min). The results revealed that the treatability of the ‎batch mode was more effective compared to the continuous mode. In the batch process, the organic ‎contaminant was completely removed compared to 82% obtained when the continuous system was ‎performed. The optimization process showed that the optimal values of the operating variables in the ‎case of the batch removal of RR-dye were 3, 78 ppm, 90 min, 20 ppm, and 60oC for pH, hydrogen ‎peroxide, irradiation time, ferrous sulfate, and temperature, respectively. Moreover, the reversion F-value ‎was 21.69, the probability P value was less than 0.001, and the correlation coefficient was (R2=0.9455), ‎which illustrates the significance of the model obtained for the batch process.‎Ali A. HassanForat Yasir AlJaberiRaid ‎ T. Al-KhateebPolish Society of Ecological Engineering (PTIE)articledyeswastewater treatmentadvanced oxidation processescentral composite designoptimizationEnvironmental technology. Sanitary engineeringTD1-1066Environmental sciencesGE1-350ENJournal of Ecological Engineering, Vol 23, Iss 1, Pp 14-23 (2022)
institution DOAJ
collection DOAJ
language EN
topic dyes
wastewater treatment
advanced oxidation processes
central composite design
optimization
Environmental technology. Sanitary engineering
TD1-1066
Environmental sciences
GE1-350
spellingShingle dyes
wastewater treatment
advanced oxidation processes
central composite design
optimization
Environmental technology. Sanitary engineering
TD1-1066
Environmental sciences
GE1-350
Ali A. Hassan
Forat Yasir AlJaberi
Raid ‎ T. Al-Khateeb
Batch and Continuous Photo-Fenton Oxidation of Reactive-Red Dye from Wastewater
description This paper aimed to investigate the ability of photo-Fenton technology to remove Reactive Red dye (RR-‎dye) from wastewater using batch and continuous operating modes. The batch mode of photo-Fenton ‎removal of organic content was conducted under the influence of solution pH (3-10), hydrogen peroxide ‎‎(25-100 ppm), irradiation time (20-90 min), ferrous sulfate (5-20 ppm), and temperature (25-60oC). For ‎comparison, the continuous treatment was conducted under the influence of the flow rate of the ‎contaminated solution (10, 20, 30, 40, and 50 mL/min). The results revealed that the treatability of the ‎batch mode was more effective compared to the continuous mode. In the batch process, the organic ‎contaminant was completely removed compared to 82% obtained when the continuous system was ‎performed. The optimization process showed that the optimal values of the operating variables in the ‎case of the batch removal of RR-dye were 3, 78 ppm, 90 min, 20 ppm, and 60oC for pH, hydrogen ‎peroxide, irradiation time, ferrous sulfate, and temperature, respectively. Moreover, the reversion F-value ‎was 21.69, the probability P value was less than 0.001, and the correlation coefficient was (R2=0.9455), ‎which illustrates the significance of the model obtained for the batch process.‎
format article
author Ali A. Hassan
Forat Yasir AlJaberi
Raid ‎ T. Al-Khateeb
author_facet Ali A. Hassan
Forat Yasir AlJaberi
Raid ‎ T. Al-Khateeb
author_sort Ali A. Hassan
title Batch and Continuous Photo-Fenton Oxidation of Reactive-Red Dye from Wastewater
title_short Batch and Continuous Photo-Fenton Oxidation of Reactive-Red Dye from Wastewater
title_full Batch and Continuous Photo-Fenton Oxidation of Reactive-Red Dye from Wastewater
title_fullStr Batch and Continuous Photo-Fenton Oxidation of Reactive-Red Dye from Wastewater
title_full_unstemmed Batch and Continuous Photo-Fenton Oxidation of Reactive-Red Dye from Wastewater
title_sort batch and continuous photo-fenton oxidation of reactive-red dye from wastewater
publisher Polish Society of Ecological Engineering (PTIE)
publishDate 2022
url https://doaj.org/article/f51fae76be2541c0851c58abad4e408b
work_keys_str_mv AT aliahassan batchandcontinuousphotofentonoxidationofreactivereddyefromwastewater
AT foratyasiraljaberi batchandcontinuousphotofentonoxidationofreactivereddyefromwastewater
AT raidtalkhateeb batchandcontinuousphotofentonoxidationofreactivereddyefromwastewater
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