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Efficient removal of bisphenol A from wastewaters: Catalytic wet air oxidation with Pt catalysts supported on Ce and Ce–Ti mixed oxides

  • Received: 31 October 2018 Accepted: 02 January 2019 Published: 10 January 2019
  • Catalytic wet air oxidation (CWAO) of an aqueous solution of bisphenol A (BPA) was investigated at 160 ℃ and 2.0 MPa of air in a batch reactor. Activity of supported platinum catalysts (2.5 wt%), prepared by wet impregnation, was compared with pure cerium and cerium–titanium oxide catalysts. Supported platinum catalysts showed higher activities in the removal of BPA than pure CeO2, Ce0.8Ti0.2O2 and Ce0.2Ti0.8O2. The oxidation reaction was followed the pseudo-first order rate law and the highest BPA removal, 97% and 95%, was achieved with Pt/CeO2 and Pt/Ce0.8Ti0.2O2 catalysts respectively. The CWAO of BPA aqueous solution was not a surface area specific reaction but the more important factor affecting the activity of studied catalysts was the amount of chemisorbed oxygen of these samples.

    Citation: Anne Heponiemi, Said Azalim, Tao Hu, Tuomas Vielma, Ulla Lassi. Efficient removal of bisphenol A from wastewaters: Catalytic wet air oxidation with Pt catalysts supported on Ce and Ce–Ti mixed oxides[J]. AIMS Materials Science, 2019, 6(1): 25-44. doi: 10.3934/matersci.2019.1.25

    Related Papers:

  • Catalytic wet air oxidation (CWAO) of an aqueous solution of bisphenol A (BPA) was investigated at 160 ℃ and 2.0 MPa of air in a batch reactor. Activity of supported platinum catalysts (2.5 wt%), prepared by wet impregnation, was compared with pure cerium and cerium–titanium oxide catalysts. Supported platinum catalysts showed higher activities in the removal of BPA than pure CeO2, Ce0.8Ti0.2O2 and Ce0.2Ti0.8O2. The oxidation reaction was followed the pseudo-first order rate law and the highest BPA removal, 97% and 95%, was achieved with Pt/CeO2 and Pt/Ce0.8Ti0.2O2 catalysts respectively. The CWAO of BPA aqueous solution was not a surface area specific reaction but the more important factor affecting the activity of studied catalysts was the amount of chemisorbed oxygen of these samples.


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    [1] Corrales J, Kristofco LA, Steele WB, et al. (2015) Global assessment of bisphenol A in the environment: Review and analysis of its occurrence and bioaccumulation. Dose-Response 13: 1559325815598308.
    [2] Meeker JD, Calafat AM, Hauser R (2010) Urinary bisphenol A concentrations in relation to serum thyroid and reproductive hormone levels in men from an infertility clinic. Environ Sci Technol 44: 1458–1463. doi: 10.1021/es9028292
    [3] Hassan ZK, Elobeid MA, Virk P, et al. (2012) Bisphenol A induces hepatotoxicity through oxidative stress in rat model. Oxid Med Cell Longev 2012: 194829.
    [4] Helmestam M, Davey E, Stavreus-Evers A, et al. (2014) Bisphenol A affects human endometrial endothelial cell angiogenic activity in vitro. Reprod Toxicol 46: 69–76. doi: 10.1016/j.reprotox.2014.03.002
    [5] Li Y, Jin F, Wang C, et al. (2015) Modification of bentonite with cationic surfactant for the enhanced retention of bisphenol A from landfill leachate. Environ Sci Pollut R 22: 8618–8628. doi: 10.1007/s11356-014-4068-0
    [6] Rocha S, Domingues V, Pinho C, et al. (2013) Occurrence of bisphenol A, estrone, 17β-estradiol and 17α-ethinylestradiol in Portuguese Rivers. B Environ Contam Tox 90: 73–78. doi: 10.1007/s00128-012-0887-1
    [7] Lee CC, Jiang LY, Kuo YL, et al. (2013) The potential role of water quality parameters on occurrence of nonylphenol and bisphenol A and identification of their discharge sources in the river ecosystems. Chemosphere 91: 904–911.
    [8] Kawagoshi Y, Fujita Y, Kishi I, et al. (2003) Estrogenic chemicals and estrogenic activity in leachate from municipal waste landfill determined by yeast two-hybrid assay. J Environ Monitor 5: 269–274. doi: 10.1039/b210962j
    [9] Coors A, Jones P, Giesy J, et al. (2003) Removal of estrogenic activity from municipal waste landfill leachate assessed with a bioassay based on reporter gene expression. Environ Sci Technol 37: 3430–3434. doi: 10.1021/es0300158
    [10] Lee H, Peart TE, Chan J, et al. (2004) Occurrence of endocrine-disrupting chemicals in sewage and sludge samples in Toronto, Canada. Water Qual Res J Can 39: 57–63. doi: 10.2166/wqrj.2004.009
    [11] Hoigné J, Bader H, Haag WR, et al. (1985) Rate constants of reactions of ozone with organic and inorganic compounds in water-III. Inorganic compounds and radicals. Water Res 19: 993–1004.
    [12] Spivack J, Leib TK, Lobos JH (1994) Novel pathway for bacterial metabolism of bisphenol A. Rearrangements and stilbene cleavage in bisphenol A metabolism. J Biol Chem 269: 7323–7329.
    [13] Marttinen SK, Kettunen RH, Rintala JA (2003) Occurrence and removal of organic pollutants in sewages and landfill leachates. Sci Total Environ 301: 1–12. doi: 10.1016/S0048-9697(02)00302-9
    [14] Clara M, Strenn B, Saracevic E, et al. (2004) Adsorption of bisphenol-A, 17β-estradiole and 17α-ethinylestradiole to sewage sludge. Chemosphere 56: 843–851. doi: 10.1016/j.chemosphere.2004.04.048
    [15] Kondrakov AO, Ignatev AN, Frimmel FH, et al. (2014) Formation of genotoxic quinones during bisphenol A degradation by TiO2 photocatalysis and UV photolysis: A comparative study. Appl Catal B-Environ 160: 106–114.
    [16] Richard J, Boergers A, vom Eyser C, et al. (2014) Toxicity of the micropollutants bisphenol A, ciprofloxacin, metoprolol and sulfamethoxazole in water samples before and after the oxidative treatment. Int J Hyg Envir Heal 217: 506–514. doi: 10.1016/j.ijheh.2013.09.007
    [17] Juhola R, Heponiemi A, Tuomikoski S, et al. (2017) Preparation of novel Fe catalysts from industrial by-products: Catalytic wet peroxide oxidation of bisphenol A. Top Catal 60: 1387–1400. doi: 10.1007/s11244-017-0829-6
    [18] Erjavec B, Kaplan R, Djinovic P, et al. (2013) Catalytic wet air oxidation of bisphenol A model solution in a trickle-bed reactor over titanate nanotube-based catalysts. Appl Catal B-Environ 132–133: 342–352.
    [19] Levec J, Pintar A (2007) Catalytic wet-air oxidation processes: A review. Catal Today 124: 172–184.
    [20] Luck F (1999) Wet air oxidation: Past, present and future. Catal Today 53: 81–91.
    [21] Sassi H, Lafaye G, Amor HB, et al. (2017) Wastewater treatment by catalytic wet air oxidation process over Al–Fe pillared clays synthesized using microwave irradiation. Front Env Sci Eng 12: 2–7.
    [22] De Los Monteros AE, Lafaye G, Cervantes A, et al. (2015) Catalytic wet air oxidation of phenol over metal catalyst (Ru, Pt) supported on TiO2–CeO2 oxides. Catal Today 258: 564–569. doi: 10.1016/j.cattod.2015.01.009
    [23] Zhang Y, Zhou Y, Peng C, et al. (2018) Enhanced activity and stability of copper oxide/γ-alumina catalyst in catalytic wet-air oxidation: Critical roles of cerium incorporation. Appl Surf Sci 436: 981–988. doi: 10.1016/j.apsusc.2017.12.036
    [24] Schmit F, Bois L, Chassagneux F, et al. (2015) Catalytic wet air oxidation of methylamine over supported manganese dioxide catalysts. Catal Today 258: 570–575. doi: 10.1016/j.cattod.2014.12.034
    [25] Yang S, Zhu W, Wang J, et al. (2008) Catalytic wet air oxidation of phenol over CeO2–TiO2 catalyst in the batch reactor and the packed-bed reactor. J Hazard Mater 153: 1248–1253. doi: 10.1016/j.jhazmat.2007.09.084
    [26] Yang S, Zhu W, Jiang Z, et al. (2006) The surface properties and the activities in catalytic wet air oxidation over CeO2–TiO2 catalysts. Appl Surf Sci 252: 8499–8505. doi: 10.1016/j.apsusc.2005.11.067
    [27] Saroha AK (2017) Treatment of industrial organic raffinate containing pyridine and its derivatives by coupling of catalytic wet air oxidation and biological processes. J Clean Prod 162: 973–981. doi: 10.1016/j.jclepro.2017.06.066
    [28] Yadav A, Verma N (2018) Carbon bead-supported copper-dispersed carbon nanofibers: An efficient catalyst for wet air oxidation of industrial wastewater in a recycle flow reactor. J Ind Eng Chem 67: 448–460. doi: 10.1016/j.jiec.2018.07.019
    [29] Kim K, Ihm S (2011) Heterogeneous catalytic wet air oxidation of refractory organic pollutants in industrial wastewaters: A review. J Hazard Mater 186: 16–34. doi: 10.1016/j.jhazmat.2010.11.011
    [30] Gaálová J, Barbier J, Rossignol S (2010) Ruthenium versus platinum on cerium materials in wet air oxidation of acetic acid. J Hazard Mater 181: 633–639. doi: 10.1016/j.jhazmat.2010.05.059
    [31] Wang J, Zhu W, He X, et al. (2008) Catalytic wet air oxidation of acetic acid over different ruthenium catalysts. Catal Commun 9: 2163–2167. doi: 10.1016/j.catcom.2008.04.019
    [32] Azalim S, Franco M, Brahmi R, et al. (2011) Removal of oxygenated volatile organic compounds by catalytic oxidation over Zr–Ce–Mn catalysts. J Hazard Mater 188: 422–427. doi: 10.1016/j.jhazmat.2011.01.135
    [33] Kolaczkowski ST, Plucinski P, Beltran FJ, et al. (1999) Wet air oxidation: A review of process technologies and aspects in reactor design. Chem Eng J 73: 143–160. doi: 10.1016/S1385-8947(99)00022-4
    [34] International Centre for Diffraction Data (ICDD) (2013) PDF-4+ powder diffraction database. 12 Campus Boulevard Newton Square, PA 19073-3273, USA.
    [35] El Fallah J, Hilaire L, Roméo M, et al. (1995) Effect of surface treatments, photon and electron impacts on the ceria 3d core level. J Electron Spectrosc 73: 89–103. doi: 10.1016/0368-2048(94)02266-6
    [36] Park PW, Ledford JS (1996) Effect of crystallinity on the photoreduction of cerium oxide:  A study of CeO2 and Ce/Al2O3 catalysts. Langmuir 12: 1794–1799.
    [37] Zhao B, Shi B, Zhang X, et al. (2011) Catalytic wet hydrogen peroxide oxidation of H-acid in aqueous solution with TiO2–CeO2 and Fe/TiO2–CeO2 catalysts. Desalination 268: 55–59. doi: 10.1016/j.desal.2010.09.050
    [38] Zhang XH, Luo LT, Duan ZH (2005) Preparation and application of Ce-doped mesoporous TiO2 oxide. React Kinet Catal Lett 87: 43–50. doi: 10.1007/s11144-006-0007-5
    [39] Francisco MSP, Mastelaro VR, Nascente PAP, et al. (2001) Activity and characterization by XPS, HR-TEM, raman spectroscopy, and BET surface area of CuO/CeO2–TiO2 catalysts. J Phys Chem B 105: 10515–10522. doi: 10.1021/jp0109675
    [40] Dipti SS, Chung UC, Chung WS (2007) Characteristics of the carbon nanotubes supported Pt–Ni and Ni electrocatalysts for DMFC. Met Mater Int 13: 257–260. doi: 10.1007/BF03027814
    [41] Luo N, Fu X, Cao F, et al. (2008) Glycerol aqueous phase reforming for hydrogen generation over Pt catalyst-Effect of catalyst composition and reaction conditions. Fuel 87: 3483–3489. doi: 10.1016/j.fuel.2008.06.021
    [42] Shyu JZ, Weber WH, Gandhi HS (1988) Surface characterization of alumina-supported ceria. J Phys Chem 92: 4964–4970. doi: 10.1021/j100328a029
    [43] Laachir A, Perrichon V, Badri A, et al. (1991) Reduction of CeO2 by hydrogen. Magnetic susceptibility and Fourier-transform infrared, ultraviolet and X-ray photoelectron spectroscopy measurements. J Chem Soc Faraday Trans 87: 1601–1609.
    [44] Galtayries A, Sporken R, Riga J, et al. (1998) XPS comparative study of ceria/zirconia mixed oxides: Powders and thin film characterisation. J Electron Spectrosc 88–91: 951–956.
    [45] Dauscher A, Hilaire L, Le Normand F, et al. (1990) Characterization by XPS and XAS of supported Pt/TiO2–CeO2 catalysts. Surf Interface Anal 16: 341–346. doi: 10.1002/sia.740160173
    [46] Larsson PO, Andersson A (1998) Complete oxidation of CO, ethanol, and ethyl acetate over copper oxide supported on titania and ceria modified titania. J Catal 179: 72–89. doi: 10.1006/jcat.1998.2198
    [47] Larachi F, Pierre J, Adnot A, et al. (2002) Ce 3d XPS study of composite CexMn1−xO2−y wet oxidation catalysts. Appl Surf Sci 195: 236–250. doi: 10.1016/S0169-4332(02)00559-7
    [48] Alifanti M, Baps B, Blangenois N, et al. (2003) Characterization of CeO2–ZrO2 mixed oxides. comparison of the citrate and sol–gel preparation methods. Chem Mater 15: 395–403.
    [49] Bedrane S, Descorme C, Duprez D (2002) Investigation of the oxygen storage process on ceria- and ceria–zirconia-supported catalysts. Catal Today 75: 401–405. doi: 10.1016/S0920-5861(02)00089-5
    [50] Bera P, Priolkar KR, Gayen A, et al. (2003) Ionic dispersion of Pt over CeO2 by the combustion method:  Structural investigation by XRD, TEM, XPS, and EXAFS. Chem Mater 15: 2049–2060. doi: 10.1021/cm0204775
    [51] Tiernan MJ, Finlayson OE (1998) Effects of ceria on the combustion activity and surface properties of Pt/Al2O3 catalysts. Appl Catal B-Environ 19: 23–35. doi: 10.1016/S0926-3373(98)00055-1
    [52] Hori CE, Permana H, Ng KYS, et al. (1998) Thermal stability of oxygen storage properties in a mixed CeO2–ZrO2 system. Appl Catal B-Environ 16: 105–117. doi: 10.1016/S0926-3373(97)00060-X
    [53] Ohko Y, Ando I, Niwa C, et al. (2001) Degradation of bisphenol A in water by TiO2 photocatalyst. Environ Sci Technol 35: 2365–2368. doi: 10.1021/es001757t
    [54] Mezohegyi G, Erjavec B, Kaplan R, et al. (2013) Removal of bisphenol A and its oxidation products from aqueous solutions by sequential catalytic wet air oxidation and biodegradation. Ind Eng Chem Res 52: 9301–9307. doi: 10.1021/ie400998t
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