Optimization of the petroleum wastewater treatment process using TiO2/Zn photocatalyst
The present study was conducted to investigate the optimum conditions in a laboratory work for the real petroleum wastewater treatment plant using both new methods (TiO2/ZnO/Fenton/Solar and TiO2/ZnO/Air/Solar) to remove Chemical Oxygen Demand (COD) and Total Organic Carbon (TOC) from the real petro...
Main Authors: | , |
---|---|
Format: | Article |
Language: | English |
Published: |
Elsevier
2021-10-01
|
Series: | South African Journal of Chemical Engineering |
Subjects: | |
Online Access: | http://www.sciencedirect.com/science/article/pii/S1026918521000457 |
_version_ | 1818726158638776320 |
---|---|
author | Dheeaa al deen Atallah Aljuboury Feroz Shaik |
author_facet | Dheeaa al deen Atallah Aljuboury Feroz Shaik |
author_sort | Dheeaa al deen Atallah Aljuboury |
collection | DOAJ |
description | The present study was conducted to investigate the optimum conditions in a laboratory work for the real petroleum wastewater treatment plant using both new methods (TiO2/ZnO/Fenton/Solar and TiO2/ZnO/Air/Solar) to remove Chemical Oxygen Demand (COD) and Total Organic Carbon (TOC) from the real petroleum wastewater from the Sohar oil refinery (SOR). Maximum treatment efficiency was obtained by the TiO2/ZnO/air/Solar process. The ZnO dosage of 54 g/L and TiO2 dosage 50 g/L were required for removing 74% of COD and 99% of TOC under optimal conditions. The solar photocatalyst of TiO2/ZnO/Fenton method was the most efficient in the neutral pH, therefore no need to adjust pH during this treatment. In acidic conditions, the solar photo-Fenton process was more efficient than the TiO2/ZnO/air process while it was less efficient than the TiO2/ZnO/air process in (pH>7). The Fe+2 and H2O2 concentration were the main factors to improve the efficiency of the TiO2/ZnO/Fenton/Solar process while pH and the TiO2 dosage were the main factors for the TiO2/ZnO/air/Solar process. The estimated cost of treatment for the TiO2/ZnO/air process was 9 $/m3 while it was 8 $/m3 by the TiO2/ZnO/Fenton process. The final expected effluent concentrations met the acceptable levels of COD and TOC set by the Wastewater Discharge Standard of Oman. |
first_indexed | 2024-12-17T21:53:46Z |
format | Article |
id | doaj.art-96ce794046cd467abfcf4b32b7526d8e |
institution | Directory Open Access Journal |
issn | 1026-9185 |
language | English |
last_indexed | 2024-12-17T21:53:46Z |
publishDate | 2021-10-01 |
publisher | Elsevier |
record_format | Article |
series | South African Journal of Chemical Engineering |
spelling | doaj.art-96ce794046cd467abfcf4b32b7526d8e2022-12-21T21:31:11ZengElsevierSouth African Journal of Chemical Engineering1026-91852021-10-01386169Optimization of the petroleum wastewater treatment process using TiO2/Zn photocatalystDheeaa al deen Atallah Aljuboury0Feroz Shaik1School of Civil Engineering, Universiti Sains Malaysia, Nibong Tebal, Pulau Pinang, Malaysia; Corresponding author.Prince Mohammad Bin Fahd University, Al Khobar, Kingdom of Saudi Arabia, Saudi ArabiaThe present study was conducted to investigate the optimum conditions in a laboratory work for the real petroleum wastewater treatment plant using both new methods (TiO2/ZnO/Fenton/Solar and TiO2/ZnO/Air/Solar) to remove Chemical Oxygen Demand (COD) and Total Organic Carbon (TOC) from the real petroleum wastewater from the Sohar oil refinery (SOR). Maximum treatment efficiency was obtained by the TiO2/ZnO/air/Solar process. The ZnO dosage of 54 g/L and TiO2 dosage 50 g/L were required for removing 74% of COD and 99% of TOC under optimal conditions. The solar photocatalyst of TiO2/ZnO/Fenton method was the most efficient in the neutral pH, therefore no need to adjust pH during this treatment. In acidic conditions, the solar photo-Fenton process was more efficient than the TiO2/ZnO/air process while it was less efficient than the TiO2/ZnO/air process in (pH>7). The Fe+2 and H2O2 concentration were the main factors to improve the efficiency of the TiO2/ZnO/Fenton/Solar process while pH and the TiO2 dosage were the main factors for the TiO2/ZnO/air/Solar process. The estimated cost of treatment for the TiO2/ZnO/air process was 9 $/m3 while it was 8 $/m3 by the TiO2/ZnO/Fenton process. The final expected effluent concentrations met the acceptable levels of COD and TOC set by the Wastewater Discharge Standard of Oman.http://www.sciencedirect.com/science/article/pii/S1026918521000457Refinery wastewaterThe TiO2/ZnO/Fenton/Solar methodThe TiO2/ZnO/Air/Solar mehodAdvanced oxidation process (AOPs) |
spellingShingle | Dheeaa al deen Atallah Aljuboury Feroz Shaik Optimization of the petroleum wastewater treatment process using TiO2/Zn photocatalyst South African Journal of Chemical Engineering Refinery wastewater The TiO2/ZnO/Fenton/Solar method The TiO2/ZnO/Air/Solar mehod Advanced oxidation process (AOPs) |
title | Optimization of the petroleum wastewater treatment process using TiO2/Zn photocatalyst |
title_full | Optimization of the petroleum wastewater treatment process using TiO2/Zn photocatalyst |
title_fullStr | Optimization of the petroleum wastewater treatment process using TiO2/Zn photocatalyst |
title_full_unstemmed | Optimization of the petroleum wastewater treatment process using TiO2/Zn photocatalyst |
title_short | Optimization of the petroleum wastewater treatment process using TiO2/Zn photocatalyst |
title_sort | optimization of the petroleum wastewater treatment process using tio2 zn photocatalyst |
topic | Refinery wastewater The TiO2/ZnO/Fenton/Solar method The TiO2/ZnO/Air/Solar mehod Advanced oxidation process (AOPs) |
url | http://www.sciencedirect.com/science/article/pii/S1026918521000457 |
work_keys_str_mv | AT dheeaaaldeenatallahaljuboury optimizationofthepetroleumwastewatertreatmentprocessusingtio2znphotocatalyst AT ferozshaik optimizationofthepetroleumwastewatertreatmentprocessusingtio2znphotocatalyst |