研究生: |
葉俊毅 Jun-Yi Yeh |
---|---|
論文名稱: |
複合高級氧化程序礦化水中低濃度異丙醇之研究 Study on Mineralization of Low-concentration Aqueous Isopropanol via Composite Advanced Oxidation Process |
指導教授: |
曾堯宣
Yao-Hsuan Tseng |
口試委員: |
顧洋
Young Ku 李豪業 Hao-Yeh Lee 陳世勛 Shih-Hsun Chen |
學位類別: |
碩士 Master |
系所名稱: |
工程學院 - 化學工程系 Department of Chemical Engineering |
論文出版年: | 2020 |
畢業學年度: | 109 |
語文別: | 中文 |
論文頁數: | 109 |
中文關鍵詞: | 金屬改質二氧化鈦 、異丙醇 、光催化降解 、高級氧化程序 |
外文關鍵詞: | Metal-modified titania, Isopropanol, Photodegradation, Advanced Oxidation Processes |
相關次數: | 點閱:300 下載:0 |
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在光電半導體產業的快速發展下,有機溶劑的需求量日益增加,有機汙染物排放量增多造成環境的污染,在水資源逐漸缺少情況下,目前發展低成本高效率的水回用處理系統是循環經濟的重要課題。
本研究利用錳改質之二氧化鈦溶膠,以含浸法將二氧化鈦鍍於陶瓷基材上,並結合UV/H2O2/O3氧化程序來降解水中低濃度異丙醇,並探討反應參數(過氧化氫濃度、氣體流量、觸媒含量、金屬元素改質)對去除效率的影響。進一步以X光繞射儀、掃描式電子顯微鏡、紫外-可見光光譜儀與螢光光譜儀對觸媒材料進行分析,以確認改質後物化特性與反應活性之關聯性。
實驗結果顯示,應用Mn-TiO2/H2O2/O3的批次反應器中,可將30ppm異丙醇在60分鐘內達成99.9%之礦化率,並進一步應用填充床反應器來模擬實場處理情況,在滯留時間30與60分鐘下,可穩定達到99.9%之異丙醇降解率及70.6%、64.0%之礦化率。因此,本系統可以做為實際反應器設計的參考,應用於高科技產業之水回用系統。
The demand of organic solvents is increasing gradually due to the ever-expanding optoelectronic and semiconductor industries, resulting in the increase in discharge of organic pollutants. The lack of water resources promotes the development of low-cost and high-efficiency water-recovery system, which is an important issue in the circular economy.
In this work, the photocatalytic ceramic filter was prepared by using the Mn-containing titania sol via impregnation process. It was applied in the degradation of low-concentration isopropanol (IPA) in water with combining UV/H2O2/O3 oxidation processes. The effect of operating parameters, such as concentration of hydrogen peroxide, gas flow rate, catalyst content, manganese- modification, on reaction rate was discussed, respectively. The manganese species on the TiO2 surface, evidenced from X-ray diffractometry (XRD), scanning electron microscope (SEM), UV-VIS spectroscopy, and fluorescence spectrometer (PL), was inferred as an important factor for the increase in mineralization rate of IPA.
Finally, the 99.9% of mineralization for 30ppm IPA was achieved after 60 min in a batch reactor, equipped with Mn-TiO2/H2O2/O3 system. A packed bed was further designed for degradation of IPA-containing water, which was applied to simulate the field condition. The conversion of IPA was higher than 99.9% both in the retention time of 30 and 60 min. The mineralization ratios were 70.6% and 64.0%, respectively. The system can be used as a reference for the filed design, which can be applied to recycle water in high tech industries.
[1] 經濟部工業局,“高科技產業揮發性廢氣處理技術及操作處理成本”,(2002)。檢自https://proj.ftis.org.tw/eta/tech/Tair005.pdf
[2] S. Woodley, & C. Catlow,“Structure prediction of titania phases: Implementation of Darwinian versus Lamarckian concepts in an Evolutionary Algorithm,”Comput. Mater. Sci., Vol. 45, pp. 84-95 (2009).
[3] F. M. Hossain, L. Sheppard, J. Nowotny, & G. E. Murch,“Optical properties of anatase and rutile titanium dioxide: Ab initio calculations for pure and anion-doped material,”J. Phys. Chem. Solids,Vol. 69, pp. 1820-1828, (2008).
[4] S. D. Mo, & W. Ching,“Electronic and optical properties of three phases of titanium dioxide: Rutile, anatase, and brookite,”Phys. Rev. B, Vol. 51, pp. 13023-13032, (1995).
[5] 薛明軒,鉑改質光觸媒二氧化鈦之紫外光與可見光應答光催化活性,國立臺灣科技大學化學工程系碩士論文,(2011)。
[6] 高嘉妤,TiO2共摻雜B/V光觸媒於管柱流反應器光降解異丙醇有機溶劑蒸氣之研究,長庚大學化工與材料工程學系碩士論文,(2017)。
[7] 洪楨琳,溫度與濕度對光催化分解苯蒸氣之影響研究,國立中山大學環境工程研究所碩士論文,(2001)。
[8] R. S. Horng, & I. C. Tseng,“Regeneration of granular activated carbon saturated with acetone and isopropyl alcohol via a recirculation process under H2O2/UV oxidation,”J. Hazard. Mater, Vol. 154, pp. 366-372, (2008).
[9] J. Medina-Valtierra, C. Frausto-Reyes, G. Camarillo-Martínez, & J. A. Ramírez-Ortiz,“Complete oxidation of isopropanol over Cu4O3 (paramelaconite) coating deposited on fiberglass by CVD,”Appl. Catal., A, Vol. 356, pp. 36-42, (2009).
[10] S. Chavadej, P. Phuaphromyod, E. Gulari, P. Rangsunvigit, & T. Sreethawong,“Photocatalytic degradation of 2-propanol by using Pt/TiO2 prepared by microemulsion technique,”Chem. Eng. J., Vol. 137, pp. 489-495, (2008).
[11] J. Wu, J. Yang, M. Muruganandham, & C. Wu,“The oxidation study of 2-propanol using ozone-based advanced oxidation processes,”Sep. Purif. Technol., Vol. 62, pp. 39-46, (2008).
[12] A. Fujishima, T. N. Rao, & D. A. Tryk, “Titanium dioxide photocatalysis,”J. Photochem. Photobiol., C, Vol. 1, pp. 1-21, (2000).
[13] E. Neyens, & J. Baeyens,“A review of classic Fenton’s peroxidation as an advanced oxidation technique,”J. Hazard. Mater., Vol. 98, pp. 33-50, (2003).
[14] K. L. Kelley, M. C. Marley, & K. L. Sperry (2003). In SituChemical Oxidation. In E. E. Moyer & P. T. Kostecki (Eds.), MTBE Remediation Handbook (pp. 223-241). Boston, MA: Springer US.
[15] 巫玉娟,活性碳纖維塗覆二氧化鈦光觸媒去除揮發性有機物之可行性研究,國立中山大學環境工程研究所碩士論文,(2005)。
[16] S. Guittonneau, J. De Laat, J. Duguet, C. Bonnel, & M. Dore,“Oxidation of parachloronitrobenzene in dilute aqueous solution by O3+ UV and H2O2+ UV: a comparative study,”Ozone: Sci. Eng., Vol,12, pp,73-94, (1990).
[17] A. Hong, M. E. Zappi, C. H. Kuo, & D. Hill,“Modeling kinetics of illuminated and dark advanced oxidation processes,”J. Environ. Eng., Vol. 122, pp. 58-62, (1996).
[18] F. Banat, S. Al-Asheh, & M. Nusair,“Photodegradation of methylene blue dye by the UV/H2O2 and UV/acetone oxidation processes,”Desalination, Vol. 181, pp. 225-232, (2005).
[19] Y. Lee, C. Lee, & J. Yoon,“Kinetics and mechanisms of DMSO (dimethylsulfoxide) degradation by UV/H2O2 process,”Water Res., Vol. 38, pp. 2579-2588, (2004).
[20] M. I. Stefan, A. R. Hoy, & J. R. Bolton,“Kinetics and mechanism of the degradation and mineralization of acetone in dilute aqueous solution sensitized by the UV photolysis of hydrogen peroxide,”Environ. Sci. Technol., Vol. 30, pp. 2382-2390, (1996).
[21] M. I. Stefan, & J. R. Bolton,“Reinvestigation of the acetone degradation mechanism in dilute aqueous solution by the UV/H2O2 process,”Environ. Sci. Technol., Vol. 33, pp. 870-873, (1999).
[22] J. Gong, Y. Liu, & X. Sun,“O3 and UV/O3 oxidation of organic constituents of biotreated municipal wastewater,”Water Res, vol. 42, pp. 1238-1244, (2008).
[23] E. Illés, E. Szabó, E. Takács, L. Wojnárovits, A. Dombi, & K. Gajda-Schrantz,“Ketoprofen removal by O3 and O3/UV processes: Kinetics, transformation products and ecotoxicity,”Sci. Total Environ., Vol. 472, pp. 178-184, (2014).
[24] D. Šojić V. Despotovic, D. Orcˇic, E. Szabó, E. Arany, S. Armakovic, E. Illés, K. Gajda-Schrantz, A. Dombi, T. Alapi, E. Sajben-Nagy, A. Palágyi, Cs. Vágvölgyi, L. Manczinger, L. Bjelica, & B. Abramovi,“Degradation of thiamethoxam and metoprolol by UV, O3 and UV/O3 hybrid processes: Kinetics, degradation intermediates and toxicity,”J. Hydrol., Vol. 472, pp. 314-327, (2012).
[25] C. Bai, X. Xiong, W. Gong, D. Feng, X. Mo, Z. Ge, & R. Xu,“Removal of rhodamine B by ozone-based advanced oxidation process,”Desalination, Vol. 278, pp. 84-90, (2011).
[26] H. Zhan, & H. Tian,“Photocatalytic degradation of acid azo dyes in aqueous TiO2 suspension I. The effect of substituents,”Dyes Pigm., Vol. 37, pp. 231-239, (1998).
[27] B. Szczepanik,“Photocatalytic degradation of organic contaminants over clay-TiO2 nanocomposites: A review,”Appl. Clay Sci., Vol. 141, pp. 227-239, (2017).
[28] L. G. Devi, & R. Kavitha,“A review on non metal ion doped titania for the photocatalytic degradation of organic pollutants under UV/solar light: role of photogenerated charge carrier dynamics in enhancing the activity,”Appl. Catal., B, Vol. 140, pp. 559-587, (2013).
[29] S. Leong, A. Razmjou, K. Wang, K. Hapgood, X. Zhang, & H. Wang,“TiO2 based photocatalytic membranes: a review,”J. Membr. Sci., Vol. 472, pp. 167-184, (2014).
[30] M. R. Sohrabi, & M. Ghavami,“Photocatalytic degradation of Direct Red 23 dye using UV/TiO2: Effect of operational parameters,”J. Hazard. Mater., Vol. 153, pp. 1235-1239, (2008).
[31] H. T. T. Tran, H. Kosslick,M. F. Ibad, C. Fischer, U. Bentrup, T. H. Vuong, L. Q. Nguyen, & A. Schulz,“Photocatalytic performance of highly active brookite in the degradation of hazardous organic compounds compared to anatase and rutile,”Appl. Catal., B, Vol. 200, pp. 647-658, (2017).
[32] R. Chauhan, A. Kumar, & R. P. Chaudhary, “Structural and photocatalytic studies of Mn doped TiO2 nanoparticles,”Spectrochim. Acta, Part A, Vol. 98, pp. 256-264, (2012).
[33] H. Feng, M.-H. Zhang, & E. Y. Liya,“Hydrothermal synthesis and photocatalytic performance of metal-ions doped TiO2,”Appl. Catal., A, Vol. 413, pp. 238-244, (2012).
[34] L. Gnanasekaran, R. Hemamalini, R. Saravanan, K. Ravichandran, F. Gracia, & V. K. Gupta,“Intermediate state created by dopant ions (Mn, Co and Zr) into TiO2 nanoparticles for degradation of dyes under visible light,” J. Mol. Liq. Vol. 223, pp. 652-659, (2016).
[35] T. El-Morsi, & M. Nanny. (2004)“Photocatalytic Degradation of Isopropanol and Acetone in Aqueous Solutions as a Function of pH and TiO2 Photocatalyst,”Proceedings of the Ninth Biennial ASCE Aerospace Division International Conference on Engineering, Construction, and Operations in Challenging Environments, pp. 407-412.
[36] D. Brinkley, & T. Engel,“Photocatalytic dehydrogenation of 2-propanol on TiO2 (110),”J. Phys. Chem. B,Vol. 102, pp. 7596-7605, (1998).
[37] 蔡沛珺,錳改質二氧化鈦於真空紫外光下降解甲苯之研究,國立臺灣科技大學化學工程系碩士論文,(2013)。
[38] 紀尚宏,鉑改質二氧化鈦於光催化程序去除液相低濃度氨氮之研究,國立臺灣科技大學化學工程系碩士論文,(2016)。
[39] G. A. Mekhemer,“Surface acid–base properties of holmium oxide catalyst: in situ infrared spectroscopy,”Appl. Catal., A, Vol. 275, pp. 1-7, (2004).
[40] H. Yao, P. Sun, D. Minakata, J. C. Crittenden, & C. H. Huang, “Kinetics and modeling of degradation of ionophore antibiotics by UV and UV/H2O2,”Environ. Sci. Technol.,Vol. 47 pp. 4581-4589, (2013).
[41] S. Esplugas, J. Gimenez, S. Contreras, E. Pascual, & M. Rodrı́guez,“Comparison of different advanced oxidation processes for phenol degradation,”Water Res, Vol. 36, pp. 1034-1042,( 2002).
[42] J. H. Suh, & M. Mohseni,“A study on the relationship between biodegradability enhancement and oxidation of 1, 4-dioxane using ozone and hydrogen peroxide,”Water Res, Vol. 38, pp. 2596-2604, (2004).
[43] J. Suave, H. J. José, & R. d. F. P. M. Moreira,“Photocatalytic degradation of polyvinylpyrrolidone in aqueous solution using TiO2/H2O2/UV system,”Environ. Technol., Vol. 39, pp. 1404-1412, (2018).
[44] Q. Hong, D. Z. Sun, & G. Q. Chi, “Formaldehyde degradation by UV/TiO2/O3 process using continuous flow mode,”J. Environ. Sci., Vol. 19, pp. 1136-1140, (2007).
[45] H. Huang, H. huang, Q. Feng, G. Liu, Y. Zhan, M. Wu, H. Lu, Y. Shu, & D. Y.C. Leung“Catalytic oxidation of benzene over Mn modified TiO2/ZSM-5 under vacuum UV irradiation,”Appl. Catal., B, Vol. 203, pp. 870-878, (2017).
[46] H. T. Li, Q. Gao, B. Han, Z. H. Ren, K. S. Xia, & C. G. Zhou,“Partial-Redox-Promoted Mn Cycling of Mn (II)-Doped Heterogeneous Catalyst for Efficient H2O2-Mediated Oxidation,”ACS Appl. Mater. Interfaces, Vol. 9, pp. 371-380, (2016).
[47] H. Wang, L. Zhang, Z. Chen, J, Hu, S. Li, Z. Wang, J. Liu, & X. Wang,“Semiconductor heterojunction photocatalysts: design, construction, and photocatalytic performances,”Chem. Soc. Rev., Vol. 43, pp. 5234-5244, (2014).
[48] J. Shi, J. Chen, Z. Feng, T. Chen, Y. Lian, X. Wang, & C. Li,“Photoluminescence characteristics of TiO2 and their relationship to the photoassisted reaction of water/methanol mixture,”J. Phys. Chem. C, Vol. 111, pp. 693-699, (2007).
[49] H. Huang, H. Huang, L. Zhang, P. Hu, X. Ye, & D. Y. Leung,“Enhanced degradation of gaseous benzene under vacuum ultraviolet (VUV) irradiation over TiO2 modified by transition metals,”Chem. Eng. J, Vol. 259, pp. 534-541, (2015).
[50] A. Gervasini, J. Fenyvesi, & A. Auroux, “Study of the acidic character of modified metal oxide surfaces using the test of isopropanol decomposition,”Catal. Lett., Vol. 43, pp. 219-228, (1997).
[51] K. T. Lu, V. H. Nguyen, Y. H. Yu, C. C. Yu, C. S. Wu, L. M. Chang, & Y. C. Lin, “An internal-illuminated monolith photoreactor towards efficient photocatalytic degradation of ppb-level isopropyl alcohol,”Chem. Eng. J, Vol. 296, pp. 11-18, (2016).
[52] M. S. Lucas, J. A. Peres, & G. L. Puma,“Treatment of winery wastewater by ozone-based advanced oxidation processes (O3, O3/UV and O3/UV/H2O2) in a pilot-scale bubble column reactor and process economics,”Sep. Purif. Technol., Vol. 72, pp. 235-241, (2010).