ABSTRACT
In this study, a new sacrificial anode comprised of scrap iron packaged in a polyethylene mesh chamber for Furan-2-carbaldehyde removal using the electrocoagulation (EC) process was fabricated. Therefore, the influences of different operational parameters, such as solution pH, current intensity, initial Furan-2-carbaldehyde concentration, and detention time on the process performance at the batch hydraulic reactor were investigated. Due to the large surface area of the anode, the applied current intensity was low, which led to high efficiency for the Furan-2-carbaldehyde removal (> 97%) at low operating voltage and energy consumption (5.4 kWh/m3). The experimental results corresponded well to the first-order kinetic model. The mineralization values for Furan-2-carbaldehyde using the EC process were 46.5% and 75.5% for total organic carbon (TOC) and chemical oxygen demand (COD), respectively. Moreover, the EC process shows the biodegradability was significantly increased compared to the initial solution after 120 min of reaction time. Based on the LC-MS analysis, the major produced intermediates and the degradation pathway of Furan-2-carbaldehyde were proposed. Consequently, on the contrary plate electrodes, the use of scrap iron as a sacrificial anode increases efficiency and reduces the total required operating costs for energy and electrodes.
Nomenclature
AOP Advanced Oxidation Process
EC Electrocoagulation
EF Electroflotation
EO Electrooxidation
DC Direct Current
HRT Hydraulic Retention Time
LC-MS Liquid chromatography–mass spectrometry
COD Chemical Oxygen Demand (mg/L)
TOC Total Organic Carbon (mg/L)
AOS Average Oxidation State
COS Carbon Oxidation State
Acknowledgments
We are grateful to Hamadan University of Medical Sciences for providing Research materials, equipment, and fund.
Disclosure statement
No potential conflict of interest was reported by the author(s).