Cargando…

Electrooxidation Using Nb/BDD as Post-Treatment of a Reverse Osmosis Concentrate in the Petrochemical Industry

This work evaluated the performance of an electrochemical oxidation process (EOP), using boron-doped diamond on niobium substrate (Nb/BDD), for the treatment of a reverse osmosis concentrate (ROC) produced from a petrochemical wastewater. The effects of applied current density (5, 10, or 20 mA·cm(−2...

Descripción completa

Detalles Bibliográficos
Autores principales: Wohlmuth da Silva, Salatiel, Venzke, Carla Denize, Bitencourt Welter, Júlia, Schneider, Daniela Eduarda, Zoppas Ferreira, Jane, Siqueira Rodrigues, Marco Antônio, Moura Bernardes, Andréa
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2019
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6427655/
https://www.ncbi.nlm.nih.gov/pubmed/30845691
http://dx.doi.org/10.3390/ijerph16050816
_version_ 1783405260224593920
author Wohlmuth da Silva, Salatiel
Venzke, Carla Denize
Bitencourt Welter, Júlia
Schneider, Daniela Eduarda
Zoppas Ferreira, Jane
Siqueira Rodrigues, Marco Antônio
Moura Bernardes, Andréa
author_facet Wohlmuth da Silva, Salatiel
Venzke, Carla Denize
Bitencourt Welter, Júlia
Schneider, Daniela Eduarda
Zoppas Ferreira, Jane
Siqueira Rodrigues, Marco Antônio
Moura Bernardes, Andréa
author_sort Wohlmuth da Silva, Salatiel
collection PubMed
description This work evaluated the performance of an electrochemical oxidation process (EOP), using boron-doped diamond on niobium substrate (Nb/BDD), for the treatment of a reverse osmosis concentrate (ROC) produced from a petrochemical wastewater. The effects of applied current density (5, 10, or 20 mA·cm(−2)) and oxidation time (0 to 5 h) were evaluated following changes in chemical oxygen demand (COD) and total organic carbon (TOC). Current efficiency and specific energy consumption were also evaluated. Besides, the organic byproducts generated by EOP were analyzed by gas chromatography coupled to mass spectrometry (GC–MS). The results show that current densities and oxidation time lead to a COD and TOC reduction. For the 20 mA·cm(−2), changes in the kinetic regime were found at 3 h and associated to the oxidation of inorganic ions by chlorinated species. After 3 h, the oxidants act in the organic oxidation, leading to a TOC removal of 71%. Although, due to the evolution of parallel reactions (O(2), H(2)O(2,) and O(3)), the specific energy consumption also increased, the resulting consumption value of 66.5 kW·h·kg(−1) of COD is considered a low energy requirement representing lower treatment costs. These results encourage the applicability of EOP equipped with Nb/BDD as a treatment process for the ROC.
format Online
Article
Text
id pubmed-6427655
institution National Center for Biotechnology Information
language English
publishDate 2019
publisher MDPI
record_format MEDLINE/PubMed
spelling pubmed-64276552019-04-10 Electrooxidation Using Nb/BDD as Post-Treatment of a Reverse Osmosis Concentrate in the Petrochemical Industry Wohlmuth da Silva, Salatiel Venzke, Carla Denize Bitencourt Welter, Júlia Schneider, Daniela Eduarda Zoppas Ferreira, Jane Siqueira Rodrigues, Marco Antônio Moura Bernardes, Andréa Int J Environ Res Public Health Article This work evaluated the performance of an electrochemical oxidation process (EOP), using boron-doped diamond on niobium substrate (Nb/BDD), for the treatment of a reverse osmosis concentrate (ROC) produced from a petrochemical wastewater. The effects of applied current density (5, 10, or 20 mA·cm(−2)) and oxidation time (0 to 5 h) were evaluated following changes in chemical oxygen demand (COD) and total organic carbon (TOC). Current efficiency and specific energy consumption were also evaluated. Besides, the organic byproducts generated by EOP were analyzed by gas chromatography coupled to mass spectrometry (GC–MS). The results show that current densities and oxidation time lead to a COD and TOC reduction. For the 20 mA·cm(−2), changes in the kinetic regime were found at 3 h and associated to the oxidation of inorganic ions by chlorinated species. After 3 h, the oxidants act in the organic oxidation, leading to a TOC removal of 71%. Although, due to the evolution of parallel reactions (O(2), H(2)O(2,) and O(3)), the specific energy consumption also increased, the resulting consumption value of 66.5 kW·h·kg(−1) of COD is considered a low energy requirement representing lower treatment costs. These results encourage the applicability of EOP equipped with Nb/BDD as a treatment process for the ROC. MDPI 2019-03-06 2019-03 /pmc/articles/PMC6427655/ /pubmed/30845691 http://dx.doi.org/10.3390/ijerph16050816 Text en © 2019 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Wohlmuth da Silva, Salatiel
Venzke, Carla Denize
Bitencourt Welter, Júlia
Schneider, Daniela Eduarda
Zoppas Ferreira, Jane
Siqueira Rodrigues, Marco Antônio
Moura Bernardes, Andréa
Electrooxidation Using Nb/BDD as Post-Treatment of a Reverse Osmosis Concentrate in the Petrochemical Industry
title Electrooxidation Using Nb/BDD as Post-Treatment of a Reverse Osmosis Concentrate in the Petrochemical Industry
title_full Electrooxidation Using Nb/BDD as Post-Treatment of a Reverse Osmosis Concentrate in the Petrochemical Industry
title_fullStr Electrooxidation Using Nb/BDD as Post-Treatment of a Reverse Osmosis Concentrate in the Petrochemical Industry
title_full_unstemmed Electrooxidation Using Nb/BDD as Post-Treatment of a Reverse Osmosis Concentrate in the Petrochemical Industry
title_short Electrooxidation Using Nb/BDD as Post-Treatment of a Reverse Osmosis Concentrate in the Petrochemical Industry
title_sort electrooxidation using nb/bdd as post-treatment of a reverse osmosis concentrate in the petrochemical industry
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6427655/
https://www.ncbi.nlm.nih.gov/pubmed/30845691
http://dx.doi.org/10.3390/ijerph16050816
work_keys_str_mv AT wohlmuthdasilvasalatiel electrooxidationusingnbbddasposttreatmentofareverseosmosisconcentrateinthepetrochemicalindustry
AT venzkecarladenize electrooxidationusingnbbddasposttreatmentofareverseosmosisconcentrateinthepetrochemicalindustry
AT bitencourtwelterjulia electrooxidationusingnbbddasposttreatmentofareverseosmosisconcentrateinthepetrochemicalindustry
AT schneiderdanielaeduarda electrooxidationusingnbbddasposttreatmentofareverseosmosisconcentrateinthepetrochemicalindustry
AT zoppasferreirajane electrooxidationusingnbbddasposttreatmentofareverseosmosisconcentrateinthepetrochemicalindustry
AT siqueirarodriguesmarcoantonio electrooxidationusingnbbddasposttreatmentofareverseosmosisconcentrateinthepetrochemicalindustry
AT mourabernardesandrea electrooxidationusingnbbddasposttreatmentofareverseosmosisconcentrateinthepetrochemicalindustry