|
|
Electrochemical advanced oxidative degradation of amino tri (methylene phosphonic acid) |
SU Shuang-you, ZHANG Yu-ling, HU Li-li, JIN Wen-zhang, WANG Shu-qin |
Department of Environmental Science and Engineering, North China Electric Power University, Baoding 071003, China |
|
|
Abstract The degradation efficiency of the electrochemical advanced oxidation process on ATMP was explored using a plate and frame electrochemical advanced oxidation device to investigate the effects of key parameters such as solution flow rate, temperature, pH, current density, and Na2SO4 concentration value; The degradation mechanism of ATMP was explored using electron paramagnetic resonance testing, free radical quenching experiments, and ATMP degradation kinetics. The results showed that when the solution flow rate was 450mL/min, temperature was 30℃, pH was 9, current density was 300A/m2, and concentration of electrolyte Na2SO4 was 0.1mol/L, the degradation rate of ATMP was the highest, reaching 99.7% within 80minutes, the Electrochemical Advanced Oxidation Process (EAOPs) was found to effectively degrade ATMP; In operating conditions, it was observed that changes in current density, solution flow rate, and temperature could affect the ATMP degradation rate, however, a change in temperature required high energy consumption, while the solution flow rate had little impact on the degradation rate, only a change in current density offered the advantage of low energy consumption and a significant impact on the ATMP degradation rate, therefore, this system was deemed suitable for using current density as the core control parameter of the reaction; The •OH (hydroxyl radical) and SO4-• (sulfate radical) generated by the EAOPs system used in this study are both involved in the degradation of ATMP, with reaction rate constants of k•OH,ATMP=(7.50 ±0.05)×108L/(mol·s) and kSO4-•,ATMP=(5.63 ±1.20)×107L/(mol·s), respectively, the •OH (hydroxyl radical) was found to play a major role in the degradation of ATMP.
|
Received: 18 February 2024
|
|
|
|
|
[1] Tang Y M, Yang W Z, Yin X S, et al. Investigation of CaCO3 scale inhibition by PAA, ATMP and PAPEMP [J]. Desalination, 2008, 228(1-3):55-60. [2] Liu F, Zhang L, Yan X, et al. Effect of diesel on corrosion inhibitors and application of bio-enzyme corrosion inhibitors in the laboratory cooling water system [J]. Corrosion Science, 2015,93:293-300. [3] Sun S H, Wang S, Ye Y X, et al. Highly efficient removal of phosphonates from water by a combined Fe(III)/UV/co-precipitation process [J]. Water Research, 2019,153:21-28. [4] Zou C J, Zhang L, Cui Y J, et al. The Solubility of the Oil Scale Inhibitor Amino Trimethylene Phosphonic Acid in Different Binary Solvents [J]. Petroleum Science and Technology, 2013,31(19):1967- 1973. [5] Jin H C, Zhang X J, Yu Y, et al. High-performance Ti/IrO2-RhOx- TiO2/alpha-PbO2/beta-PbO2 electrodes for scale inhibitors degradation [J]. Chemical Engineering Journal, 2022,435:135167. [6] Wang S, Zhang B L, Shan C, et al. Occurrence and transformation of phosphonates in textile dyeing wastewater along full-scale combined treatment processes [J]. Water Research, 2020,184:116173. [7] Xu L H, Li J J, Zeng H B, et al. ATMP-induced three-dimensional conductive polymer hydrogel scaffold for a novel enhanced solid-state electrochemiluminescence biosensor [J]. Biosens Bioelectron, 2019, 143:7. [8] Pervov A, Andrianov A, Rudakova G, et al. A comparative study of some novel "green" and traditional antiscalants efficiency for the reverse osmotic black sea water desalination [J]. Desalination and Water Treatment, 2017,73:11-21. [9] Nowack B. Aminopolyphosphonate removal during wastewater treatment [J]. Water Research, 2002,36(18):4636-4642. [10] Forlani G, Prearo V, Wieczorek D, et al. Phosphonate degradation by spirulina strains: cyanobacterial biofilters for the removal of anticorrosive polyphosphonates from wastewater [J]. Enzyme and Microbial Technology, 2011,48(3):299-305. [11] Altaf R, Lin X C, Tadda M A, et al. Modified magnetite adsorbent (Zr-La@Fe3O4) for nitrilotrismethylenephosphonate (NTMP) removal and recovery from wastewater [J]. Journal of Cleaner Production, 2021, 278:123960. [12] Möller S, Prikler S, Einax J W. Pulse polarographic determination of the complexation capacity of various organic phosphonates of heavy metals with the aid of design of experiments [J]. Microchemical Journal, 2010,96(2):296-300. [13] Boels L, Keesman K J, Witkamp G J. Adsorption of phosphonate antiscalant from reverse osmosis membrane concentrate onto granular ferric hydroxide [J]. Environmental Science & Technology, 2012,46(17):9638-9645. [14] Schowanek D, Verstraete W. Phosphonate utilization by bacterial cultures and enrichments from environmental samples [J]. Applied and Environmental Microbiology, 1990,56(4):895-903. [15] Greenlee L F, Freeman B D, Lawler D F. Ozonation of phosphonate antiscalants used for reverse osmosis desalination: parameter effects on the extent of oxidation [J]. Chemical Engineering Journal, 2014, 244:505-513. [16] Armbruster D, Rott E, Minke R, et al. Trace-level determination of phosphonates in liquid and solid phase of wastewater and environmental samples by IC-ESI-MS/MS [J]. Analytical and Bioanalytical Chemistry, 2020,412(20):4807-4825. [17] Nowack B. The behavior of phosphonates in wastewater treatment plants of switzerland [J]. Water Research, 1998,32(4):1271-1279. [18] Huang N, Xu Z B, Wang W L, et al. Elimination of amino trimethylene phosphonic acid (ATMP) antiscalant in reverse osmosis concentrate using ozone: anti-precipitation property changes and phosphorus removal [J]. Chemosphere, 2022,291(Pt 3):133027. [19] Reinhardt T, Campero A N V, Minke R, et al. Batch studies of phosphonate and phosphate adsorption on granular ferric hydroxide (GFH) with membrane concentrate and its synthetic replicas [J]. Molecules, 2020,25(21):1-18. [20] Moreira F C, Boaventura R A R, Brillas E, et al. Electrochemical advanced oxidation processes: A review on their application to synthetic and real wastewaters [J]. Applied Catalysis B-Environmental, 2017,202:217-261. [21] Aline J M da Costa, Matheus S Kronka, Paulo J M, et al. Treatment of Tebuthiuron in synthetic and real wastewater using electrochemical flow-by reactor [J]. Journal of Electroanalytical Chemistry, 2021, 882:114978. [22] Salatiel W da Silva, Emma M O Navarro, Marco A S Rodrigues, et al. Using p-Si/BDD anode for the electrochemical oxidation of norfloxacin [J]. Journal of Electroanalytical Chemistry, 2019,832:112- 120. [23] Sanna D, Fadda A. Role of the hydroxyl radical-generating system in the estimation of the antioxidant activity of plant extracts by electron paramagnetic resonance (EPR) [J]. Molecules, 2022,27(14):1-12. [24] He P, Zhu J Y, Chen Y Z, et al. Pyrite-activated persulfate for simultaneous 2,4-DCP oxidation and Cr(VI) reduction [J]. Chemical Engineering Journal, 2021,406:126758. [25] Panizza M, Barbucci A, Ricotti R, et al. Electrochemical degradation of methylene blue [J]. Separation and Purification Technology, 2007, 54(3):382-387. [26] Samet Y, Elaoud S C, Ammar S, et al. Electrochemical degradation of 4-chloroguaiacol for wastewater treatment using PbO2 anodes [J]. Journal of Hazardous Materials, 2006,138(3):614-619. [27] Liang Z H, Fan C M, Sun Y P. Electrocatalysis of oxygen evolution reaction on Ti/SnO2+RuO2+MnO2/MnO2 electrode in sulfuric acid solution [J]. Chemical Research in Chinese Universities, 2001,(3): 287-292. [28] Yang S W, Cheng J H, Sun J, et al. Defluorination of Aqueous Perfluorooctanesulfonate by Activated Persulfate Oxidation [J]. Plos One, 2013, 8(10): 10. [29] Luu T L, Tien T T, Duong N B, et al. Study of the treatment of tannery wastewater after biological pretreatment by using electrochemical oxidation on BDD/Ti anode [J]. Desalination and Water Treatment, 2019, 137: 194-201. [30] Wang W L, Wu Q Y, Huang N, et al. Synergistic effect between UV and chlorine (UV/chlorine) on the degradation of carbamazepine: Influence factors and radical species [J]. Water Research, 2016,98: 190-198. |
|
|
|