电化学氧化耦合铁感应电极激发过硫酸盐氧化处理焦化废水生化出水
Electrochemical oxidation coupling iron plate induction electrode excited persulfate oxidation treatment of coking wastewater biochemical water
-
摘要: 采用电化学氧化(EC)耦合铁(IP)感应电极激发过硫酸盐(KPS)氧化处理焦化废水生化出水,在反应器阴、阳极之间等距离嵌入铁板构建电化学双电解反应体系.该体系中,铁板作为感应电极,充当阳极材料的同时兼具有阴极材料的作用,加快过硫酸盐的活化.在电化学氧化耦合铁感应电极激发过硫酸盐(EC/IP/KPS)试验中,分别将电解时间(0—50 min)、电流密度(0—60 mA·cm-2)和过硫酸钾(KPS)投加量(0—5 mmol·L-1)作为控制条件,探讨了在不同的影响条件下该电化学反应体系对水中COD、TOC及UV254等有机物污染指标的降解程度.在此基础上,利用SEM、EDS、XRD和XPS等对EC/IP/KPS过程中产生的絮凝物进行了表征,进而推断EC/IP/KPS系统的反应机理.结果表明,在EC/IP/KPS系统中的耦合作用下,当电解时间为30 min、电流密度为30 mA·cm-2、过硫酸钾浓度为2 mmol·L-1时,COD去除率可达77.0%、TOC去除率为54.0%,UV254值明显降低.此外,还对3种不同的实验过程进行了对比,发现EC/IP/KPS系统的处理效果要明显优于KPS和EC/IP处理体系.Abstract: Electrochemical(EC) oxidation coupling iron plate(IP) induction electrode excited persulfate(KPS) oxidation treatment of coking wastewater biochemical water. Electrochemical double electrolytic reaction system was built in the iron plate equidistantly between the reactor cathode and anode. In this system iron plate (IP) as an inductive electrode, acted as an anode material as well as a cathode material, accelerating the activation of persulfate. In an electrochemical oxidation coupled iron plate induction electrode induced persulfate test, electrolysis time (0-50 min), current density (0-60 mA·cm-2) and persulfate (KPS) addition amount (0-5 mmol·L-1) were used as the control conditions, the degradation degree of organics pollution indexes including COD, TOC and UV254 was discussed under different conditions. On this basis, the flocs produced in the EC/IP/KPS process were characterized by SEM, EDS, XRD and XPS, and the reaction mechanism of the EC/IP/KPS system was inferred. The results showed that when the electrolysis time was 30 min, the current density was 30 mA·cm-2, and the persulfate concentration was 2 mmol·L-1, the COD removal rate was 77.0%, the TOC removal rate was 54.0% and the UV254 value was reduced significantly under the coupling effect of EC/IP/KPS system. It was found that the processing effect of EC/IP/KPS system was better significantly than that of the PS and EC/IP systems, during the comparison of three different experimental processes.
-
Key words:
- coking waste water /
- electrochemistry /
- induction electrode /
- sulfate radical /
- iron
-
[1] ZHANG M, TAY J H, QIAN Y, et al. Coke plant wastewater treatment by fixed biofilm system for COD and NH3-N removal[J]. Water Research, 1998, 32(2):519-527. [2] ZHU X B, TIAN J P, LIU R, et al. Optimization of Fenton and electro-Fenton oxidation of biologically treated coking wastewater using response surface methodology[J]. Separation & Purification Technology, 2011, 81(3):444-450. [3] SHI J, DENG H, BAI Z, et al. Emission and profile characteristic of volatile organic compounds emitted from coke production, iron smelt, heating station and power plant in Liaoning Province, China[J]. Science of the Total Environment, 2015, 515-516:101-108. [4] ZHU X, NI J, LAI P. Advanced treatment of biologically pretreated coking wastewater by electrochemical oxidation using boron-doped diamond electrodes[J]. Water Research, 2009, 43(17)4347-4355. [5] ZHANG W, WEI C, FENG C, et al. The occurrence and fate of phenolic compounds in a coking wastewater treatment plant[J]. Water Science & Technology, 2013, 68(2):433-440. [6] REN Y, LI T, WEI C. Competitive adsorption between phenol, aniline andn-heptane in tailrace coking wastewater[J]. Water Air and Soil Pollution, 2013, 224(1):1365-1376. [7] ZHANG W, WEI C, CHAI X, et al. The behaviors and fate of polycyclic aromatic hydrocarbons (PAHs) in a coking wastewater treatment plant[J]. Chemosphere, 2012, 88(2):174-182. [8] BAI Y, SUN Q, SUN R, et al. Bioaugmentation and adsorption treatment of coking wastewater containing, pyridine and quinoline using zeolite-biological aerated filters[J]. Environmental Science & Technology, 2011, 45(5):1940-1948. [9] BYUNGRA L,HONGYING H, KOICHI F. Biological degradation and chemical oxidation characteristics of coke-oven waste water[J]. Water Air & Soil Pollution, 2003, 146(1-4):23-33. [10] LAI P, ZHAO H Z, ZENG M, et al. Study on treatment of coking wastewater by biofilm reactors combined with zero-valent iron process[J]. Journal of Hazardous Materials, 2009, 162(2-3):1423-1429. [11] EPOLD I, TRAPIDO M, DULOVA N. Degradation of levofloxacin in aqueous solutions by Fenton, ferrous ion-activated persulfate and combined Fenton/persulfate systems[J]. The Chemical Engineering Journal, 2015, 279:452-462. [12] LIN H, ZHONGX, CIOTONEA C, et al. Efficient Degradation of clofibric acid by electro-enhanced peroxydisulfate activation with Fe-Cu/SBA-15 catalyst[J]. Applied Catalysis B:Environmental, 2018,230:1-10. [13] 任云.电化学氧化去除剩余氨水中氨氮的应用研究[D].天津:天津大学,2015. REN Y. Study and application of ammonia electrooxidation on coking residual ammonia wastewater[D].Tianjin:Tianjing University,2015(in Chinese). [14] 胡敬,蔡铎昌,何代平.铁碳内电解法处理含酚废水[J].西华师范大学学报,2006,27(1):106-108. HU J, CAI D C, HE D P.IroN inner electrolysis processing treating phenol-containing waste water[J].Journal of China West Normal University,2006,27(1):106-108(in Chinese).
[15] LIN H, WU J, ZHANG H. Degradation of bisphenol A in aqueous solution by a novel electro/Fe3+/peroxydisulfate process[J]. Separation and Purification Technology, 2013, 117(Complete):18-23. [16] WU J, ZHANG H, QIU J. Degradation of Acid Orange 7 in aqueous solution by a novel electro/Fe2+/peroxydisulfate process[J]. Journal of Hazardous Materials, 2012, 215-216(none):138-145. [17] LIN H, ZHANG H, HOU L. Degradation of C. I. Acid Orange 7 in aqueous solution by a novel electro/Fe3O4/PDS process[J]. Journal of Hazardous Materials, 2014, 276:182-191. [18] LIANG C, LEE I L, HSU I Y, et al. Persulfate oxidation of trichloroethylene with and without iron activation in porous media[J]. Chemosphere, 2008, 70(3):426-435. [19] YUAN S, LIAO P, ALSHAWABKEH A N. Electrolytic manipulation of persulfate reactivity by iron electrodes for trichloroethylene degradation in groundwater[J]. Environmental Science & Technology, 2014, 48(1):656-663. [20] LI J, REN Y, LAI L. Electrolysis assisted persulfate with annular iron sheet as anode for the enhanced degradation of 2, 4-dinitrophenol in aqueous solution[J]. Journal of Hazardous Materials, 2017, 344:778-787. [21] DING Y, ZHU L, WANG N, et al. Sulfate radicals induced degradation of tetrabromobisphenol A with nanoscaled magnetic CuFe2O4 as a heterogeneous catalyst of peroxymonosulfate[J]. Applied Catalysis B Environmental, 2013, 129:153-162. [22] HE J, YANG X, MEN B, et al. Interfacial mechanisms of heterogeneous Fenton reactions catalyzed by iron-based materials:A review[J]. Journal of Environmental Sciences, 201539:97-109. [23] MATZEK L W, CARTER K E. Activated persulfate for organic chemical degradation:A review[J]. Chemosphere, 2016, 151:178-188. [24] YAMASHITA T, HAYES P. Analysis of XPS spectra of Fe2+ and Fe3+ ions in oxide materials[J]. Applied Surface Science, 2008, 254(8):2441-2449. [25] KUMAR S, PRAKASH R, CHOUDHARY R J, et al. Structural, XPS and magnetic studies of pulsed laser deposited Fe doped Eu2O3 thin film[J]. Materials Research Bulletin, 2015, 70:392-396. [26] XU L, WANG J. Magnetic nanoscaled Fe3O4/CeO2 composite as an efficient Fenton-like heterogeneous catalyst for degradation of 4-chlorophenol[J]. Environmental Science & Technology, 2017, 46(18):10145-10153. [27] DO S H, KWON Y J, BANG S J, et al. Persulfate reactivity enhanced by Fe2O3-MnO and CaO-Fe2O3-MnO composite:Identification of composite and degradation of CCl4 at various levels of pH[J]. Chemical Engineering Journal, 2013, 221:72-80. [28] PIUMETTI M, FINO D, RUSSO N. Mesoporous manganese oxides prepared by solution combustion synthesis as catalysts for the total oxidation of VOCs[J]. Applied Catalysis B Environmental, 2015, 163(163):277-287. [29] MERCIER F, ALLIOT C, BION L, et al. XPS study of Eu(Ⅲ) coordination compounds:Core levels binding energies in solid mixed-oxo-compounds EumXxOy[J]. Journal of Electron Spectroscopy and Related Phenomena, 2006, 150(1):21-26.
计量
- 文章访问数: 1763
- HTML全文浏览数: 1763
- PDF下载数: 41
- 施引文献: 0