| Literature DB >> 32420422 |
Fu Liu1, Wenwen Li1, Dechang Wu1, Tong Tian1, Jian-Feng Wu1, Zong-Mu Dong1, Guang-Chao Zhao1.
Abstract
The aim of this research is to degrade organic contaminants in aqueous solution via lead ferrite (PbFe2O4) as a catalyst to activate peroxymonosulfate (PMS). PbFe2O4 was synthesized by a citrate combustion method and analyzed by SEM, TEM and XRD. A simulated solution including thionine were used, with different conditions tested to optimize the degradation process, including comparing PbFe2O4 to other catalysts, PbO and Fe2O3, and tracking active oxygen species. The concentrations of thionine and PMS were tracked with a UV-Vis spectrophotometer in the treatment process. The data are presented as graphs and tables. A detailed analyses of this report can be found in the article "New insight into the mechanism of peroxymonosulfate activation by nanoscaled lead-based spinel for organic matters degradation: a singlet oxygen-dominated oxidation process" published in Journal of colloid and interface science.Entities:
Keywords: AOPs; Lead ferrite; Organic contaminants degradation; Peroxymonosulfate; non-radical process
Year: 2020 PMID: 32420422 PMCID: PMC7214939 DOI: 10.1016/j.dib.2020.105626
Source DB: PubMed Journal: Data Brief ISSN: 2352-3409
Fig. 1XRD spectra of virgin PbFe2O4 prepared with different calcination temperature (400-600°C)
Fig. 2SEM (a), TEM (b) images of the used PbFe2O4.
Fig. 3(a) Thionine removal efficiency in different systems, (b) thionine removal efficiency in catalytic PMS by PbFe2O4, Fe2O3 and PbO. General conditions: [PMS]0=400μM, Catalyst dosage=400mg•L−1, [Thionine]0=10μM, pH=9.0, T=25°C.
Fig. 4Thionine removal efficiency in using PbFe2O4/PMS system under different pH in 20min. Conditions: [Thionine]0=10μM, [PMS]0=400μM, Catalyst dosage=400mg•L−1, T=25°C.
Fig. 5Concentrations of lead and ferric ions leached from PbFe2O4/PMS system after every cycle use of PbFe2O4.
Variation of the pseudo-first order rate constant of thionine degradation with catalyst dosages in PMS oxidation system.
| Oxide dose (mg/L) | R2 | |
|---|---|---|
| 200 | 0.2002 | 0.967 |
| 400 | 0.2048 | 0.970 |
| 600 | 0.1477 | 0.981 |
| 800 | 0.1347 | 0.984 |
| 200 | 0.1172 | 0.983 |
| 400 | 0.1235 | 0.996 |
| 600 | 0.0716 | 0.992 |
| 800 | 0.0526 | 0.960 |
| 200 | 0.1027 | 0.989 |
| 400 | 0.1068 | 0.985 |
| 600 | 0.0332 | 0.913 |
| 800 | 0.0234 | 0.922 |
Variation of the pseudo-first order rate constant of thionine degradation with coexisting anions concentration in PbFe2O4/PMS system.
| Coexisting anions (mM) | R2 | |
|---|---|---|
| 0 | 0.2048 | 0.970 |
| 5 | 0.2133 | 0.955 |
| 20 | 0.2724 | 0.950 |
| 50 | 0.4231 | 0.987 |
| 100 | 0.5970 | 0.981 |
| 0 | 0.2048 | 0.970 |
| 20 | 0.1906 | 0.975 |
| 50 | 0.1991 | 0.972 |
| 0 | 0.2048 | 0.970 |
| 20 | 0.2108 | 0.965 |
| 50 | 0.2016 | 0.975 |
| 0 | 0.2048 | 0.970 |
| 20 | 0.2176 | 0.977 |
| 50 | 0.2445 | 0.994 |
Contaminants removal by advanced oxidation processes based on different catalyst/persulfates catalytic oxidation system.
| Advanced oxidation process | Target pollutant | Main reactive species | Reference |
|---|---|---|---|
| CuFe2O4/peroxymonosulfate | Arsenic(Ⅲ) | SO4•− and •OH | |
| CuFe2O4/peroxymonosulfate | Norfloxacin | SO4•− and •OH | |
| CuFe2O4/kaolinite/peroxymonosulfate | Bisphenol A | SO4•− and •OH | |
| Benzoquinone/Peroxymonosulfate | sulfamethoxazole | 1O2 | |
| CuO@CHFMs/Peroxymonosulfate | Bisphenol A | 1O2 | |
| MWCNTS/peroxymonosulfate | Methylene blue and phenol | charge transfer | |
| α-MnO2/Peroxymonosulfate | ciprofloxacin | SO4•−, •OH and 1O2 | |
| Graphitized nanodiamonds/persulfates | Various organic compounds | charge transfer | |
| Cu/CuFe2O4//persulfate | Tetracycline | SO4•− and •OH | |
| Fe3O4/sepiolite/persulfate | Atrazine | SO4•− and SO5•− | |
| CuO/peroxydisulfate | 2,4-dichlorophenol | charge transfer | |
| PbFe2O4/peroxymonosulfate | Thionine and tetracyclines | 1O2 | This work |
Fig. 6EPR spectra of TMP−1O2 and DMPO-SO4•−/•OH/O2•−.
Conditions: [PMS]0=1mM, [PbFe2O4]=400mg•L−1, pH=9.0, T=25°C, 3min, [TMP]0=25mM, [DMPO]0=25mM.
Fig. 7Remvoal efficiency of Tetracycline (a) and Metacycline (b) by PbFe2O4/PMS system in different water samples. General conditions: [Tetracyclines]0=5mg•L−1, [PMS]0=400μM, Catalyst dosage=400mg•L−1, pH=9.0, T=25°C.
| Subject | Environmental engineering |
| Specific subject area | Advanced oxidation process |
| Type of data | Table |
| How data were acquired | Field emission scanning electron microscope (FESEM, Hitachi SU-8010, 5kV, Japan), field emission transmission electron microscope (FETEM, Hitachi HT-7700, 120kV, Japan), X-ray diffraction (XRD, Bruker D8 Advance, Germany), Electron paramagnetic resonance spectrometer (EPR, Bruker Biospin GmbH E500-9.5/12, Germany), Atomic Absorption Spectrophotometer (AAS, TAS-990, China), UV-Vis spectrophotometer (TU-1901, China), and high-performance liquid chromatography (HPLC, Shimadzu LC-20AT, Japan) |
| Data format | Raw and analyzed data |
| Parameters for data collection | The effect of initial thionine concentration, solution pH, catalysts and peroxymonosulfate dosages was evaluated during the experiments of organic degradation. Experiments were done in triplicates in separate reactors and room temperature (25±2°C) was maintained throughout the reactions. |
| Description of data collection | HPLC coupled with UV detector was used to track tetracyclines antibiotics concentrations throughout the degradation reaction, and the thionine concentration of different time intervals were detected by UV-Vis spectrophotometer. |
| Data source location | Anhui Normal University |
| Data accessibility | With the article |
| Related research article | Author's name |