Determination of Operating Conditions for Hydrogen Peroxide and Hydroxyl Radical Production in Electro-peroxone Process
Abstract
Electro-peroxone (EPO) process is an enhanced ozonation process with a
simple installation of electro-oxidation apparatus into the ozone reactor. It
enables the use of excess oxygen gas caused by inefficient ozone generation by
ozone generators. The sparged oxygen is reduced to form hydrogen peroxide (H2O2)
on the cathode surface and then the electrogenerated H2O2 reacts
with ozone to form hydroxyl radical (OH•). Thus, the highly oxidative species
such as OH• and H2O2,are produced in the bulk solution. In this study, the effects
of operating conditions such as reaction time, ozone flow rate and the applied
current on the production of oxidant species were discussed. Response Surface
Methodology (RSM) was used for the modeling of reaction conditions. The models
employed were both significant for the production of OH• and H2O2.
Reaction time is the most important factor in the production of oxidants. While
the reaction time and ozone flow rate had a synergistic effect on OH•
production, the interaction of the applied flow and the ozone flow rate
affected H2O2 production. Optimum operating conditions
were determined maximizing the OH• concentration. The short reaction time of
the process may be preferred because OH• is inhibited by the electrogenerated H2O2
at advancing reaction times.
Keywords
References
- 1. Hou M., Chu Y., Li X., Wang H., Yao W., Yu G., Murayama S., Wang Y. 2016. Electro-peroxone degradation of diethyl phthalate: Cathode selection, operational parameters, and degradation mechanisms. Journal of Hazardous materials; 319: 61-68.
- 2. Munter R. 2001. Advanced oxidation processes–current status and prospects. Proceedings of the Estonian Academy of Sciences. Chemistry; 50 (2): 59-80.
- 3. Wang H., Yuan S., Zhan J., Wang Y., Yu G., Deng S., Huang J., Wang B. 2015. Mechanisms of enhanced total organic carbon elimination from oxalic acid solutions by electro-peroxone process. Water Research; 80: 20-29.
- 4. Wang H., Bakheet B., Yuan S., Li X., Yu G., Murayama S., Wang Y. 2015. Kinetics and energy efficiency for the degradation of 1, 4-dioxane by electro-peroxone process. Journal of Hazardous materials; 294: 90-98.
- 5. Guo W., Wu Q.-L., Zhou X.-J., Cao H.-O., Du J.-S., Yin R.-L., Ren N.-Q. 2015. Enhanced amoxicillin treatment using the electro-peroxone process: key factors and degradation mechanism. RSC Advances; 5 (65): 52695-52702.
- 6. Bakheet B., Yuan S., Li Z., Wang H., Zuo J., Komarneni S., Wang Y. 2013.Electro-peroxone treatment of Orange II dye wastewater. Water Research; 47 (16): 6234-6243.
- 7. Turkay O., Barışçı S., Sillanpää M. 2017. E-peroxone Process for the Treatment of Laundry Wastewater: A Case Study. Journal of Environmental Chemical Engineering; 5(5): 4282-4290.
- 8. Li Z., Yuan S., Qiu C., Wang Y., Pan X., Wang J., Wang C., Zuo J. 2013. Effective degradation of refractory organic pollutants in landfill leachate by electro-peroxone treatment. Electrochimica Acta; 102: 174-182.
Details
Primary Language
English
Subjects
Engineering
Journal Section
Research Article
Authors
Özge Dinç
*
Türkiye
Zeynep Girgin Ersoy
This is me
Hazal Öztürk
This is me
Sibel Barışçı
This is me
Publication Date
September 30, 2019
Submission Date
February 15, 2018
Acceptance Date
September 17, 2019
Published in Issue
Year 2019 Volume: 15 Number: 3