簡易檢索 / 詳目顯示

研究生: 馬漢德
Nunez, Mahasti, Nicolaus Nezha
論文名稱: 以新穎流體化床均質結晶技術處理含鈣、鋅廢水之研究
Calcium and Zinc Removal from Wastewater by a Novel Fluidized-bed Homogeneous Crystallization (FBHC) Technology
指導教授: 黃耀輝
Huang, Yao-Hui
學位類別: 碩士
Master
系所名稱: 工學院 - 化學工程學系
Department of Chemical Engineering
論文出版年: 2014
畢業學年度: 102
語文別: 英文
論文頁數: 107
外文關鍵詞: carbonate salts, fluidized bed homogeneous crystallizer, removal efficiency, cross-section loading, XRD, SEM
相關次數: 點閱:103下載:5
分享至:
查詢本校圖書館目錄 查詢臺灣博碩士論文知識加值系統 勘誤回報
  • A new process for removing metal contamination from wastewater has been developed. This work applied carbonate salts as a precipitant for homogeneously producing metal carbonate crystal without seed materials from synthetic wastewater using a fluidized bed homogeneous crystallizer (FBHC).
    In calcium removal experiment, The optimum pH of about 10 to 11. The calcium removal efficiency could achieve more than 99 % and crystallization ratio could achieve more than 93% for various initial calcium concentration (50 – 150 ppm). FBHC technology is suitable to deal with the cross-section loading of zinc wastewater below 5.5 Kg/m2hr for pH 10.8 – 11.2. The XRD analysis indicated that the calcium salt crystallization product was consisted of two calcium carbonate (CaCO3) phases, the calcite, the aragonite, and the calcium oxide (CaO). The surface morphology of SEM analysis revealed that calcium carbonate particles (around 0.8 mm) were formed by the aggregation of fine crystal (around 5 μm) layer by layer
    In a zinc removal experiment, at an optimum pH was about 9 to 10 zinc removal efficiency could achieve more than 99.9% and crystallization ratio could achieve more than 95% for various zinc concentration (50 – 150 ppm). FBHC technology could deal with the cross-section loading of zinc wastewater below 2.3 Kg/m2hr for pH 9.6 – 9.8. The XRD analysis showed that the FBHC product was a mixed phase of Smithsonite (ZnCO3) and Hydrozincite (Zn5(OH)6(CO3)2). The surface morphology of SEM analysis revealed that zinc carbonate particles (around 0.5 mm) were formed by the aggregation of fine crystal (around 4 μm).
    In mixed compound, zinc and calcium removal was held in two series FBHC because of the different optimum pH for zinc and calcium removal. The initial concentrations of zinc was 300 ppm and that of calcium was 75 and 750 ppm. Both, zinc and calcium removal could achieve above 99%. The crystallization ratio achieved 98% for zinc and 96% for calcium.
    In tap water softening process, under pH above 10.5, calcium removal achieved more than 90%. The low magnesium ions in tap water significantly affect the softening results.

    CONTENTS ABSTRACT II ACKNOWLEDGEMENT IV CONTENTS V TABLE CONTENTS VII FIGURE CONTENTS VIII CHAPTER 1 INTRODUCTION 1 1.1 Background 1 1.2 Research Objective 3 CHAPTER 2 LITERATURE REVIEW 4 2.1 Solubility Curve 7 2.1.1 Zinc Solubility Curve 7 2.1.2 Calcium Solubility Curve 12 2.1.3 Carbonate equlibrium in open system 15 2.2 FBHC Operation Condition 17 2.2.1 Fluidization 17 2.2.2 Nucleation and Crystal Growth 21 2.3 Application of FBHC for metal removal from electroplating wastewater 24 CHAPTER 3 EXPERIMENTAL METHODS 26 3.1Frame Work of the Experiment 26 3.2 Materials and analytical methods 26 3.2.1 Materials 26 3.2.2 Analytical Method 28 3.3 Experimental Instrument 30 3.4 Experimental Apparatus 34 3.5 Experimental Procedure 35 3.5.1 Metal Carbonate Crystal Synthesis 36 3.5.2 Jar Test for Metal Removal Experiments 36 3.5.3 Equilibrium Time and Adsorption Effect of The crystal Process 36 3.5.4 pH Effect in Metal Removal Process 37 3.5.5 Loading Effect in Metal Removal Process 37 3.5.6 Characterization of Metal Carbonate Crystal 38 CHAPTER 4 RESULTS AND DISCUSSION 39 4.1 Calcium Removal 39 4.1.1 Calcium Crystal Synthesis 39 4.1.2 Jar Test for Calcium Removal Experiments 41 4.1.3 Calcium Removal Mechanism 44 4.1.4 pH Effect in Calcium Removal Process 47 4.1.5 Loading effect 49 4.1.6 Product analysis 55 4.2 Zinc removal 58 4.2.1 Jar test for zinc removal 58 4.2.2 Zinc crystal synthesis 62 4.2.3 Zinc removal mechanism 64 4.2.4 pH effect in zinc removal process 67 4.2.5 Loading effect 69 4.2.6 Product Analysis 74 4.3 Zinc and calcium removal from synthetic electroplating wastewater 77 4.3.1 Jar test 77 4.3.2 XRD Analysis Results for Jar Test 82 4.3.3 Mixed Zinc and Calcium Crystal Synthesis 83 4.3.4 Zinc and Calcium Removal in FBHC 85 4.3.5 XRD Results for Mixed Metal Removal Crystal Product 101 4.3.6 SEM Results for Mixed Metal Removal Crystal Product 102 CHAPTER 5 CONCLUSIONS AND RECOMMENDATIONS 105 5.1 Conclusions 105 5.2 Recommendations 107 REFERENCE XI

    REFERENCE

    [1] www.lenntech.com/periodic/elements/ca.htm, in.
    [2] S.N. Bsc, Oxalate content of foods and its effect on humans, Asia Pacific Journal of Clinical Nutrition, 8 (1999) 64-74.
    [3] www.lenntech.com/periodic/elements/zn.htm, in.
    [4] Y.L. Qiang Liu, Jia Zhang, Ying Chi, Xiuxiu Ruan, Jianyong Liu, Guangren Qian, Effective removal of zinc from aqueous solution by hydrocalcumite, Chemical Engineering Journal, 175 (2011) 33-38.
    [5] T.W. Department, International Comparison of Water Quality, in, Taipei Water Department, Taipei, 2010.
    [6] I.M.o. Health, Peraturan Menteri kesehatan Tentang Syarat - Syarat dan Pengawasan Kualitas Air, in, Indonesia, 1990.
    [7] W.H. Organization, Background Document for Development of WHO Guidlines for Drinking Water Quality, in: Zinc in Drinking Water, World Health Organization, Geneva, 2003.
    [8] Cotruvo J, J. Bartram, Calcium and Magnesium in Drinking Water : Public Health Significance, World Health Organization (WHO), Geneva, 2009.
    [9] S. Kim, J.-Y. Park, Y.-W. Lee, J.-J. Lee, J.-Y. Choi, Y.-K. Choi, K.-W. Hwang, P. Vella, W.-K. Lee, High-rate calcium removal using the Hyperkinetic Vortex Crystallization (HVC) process for reuse of electronics wastewater, Desalination, 249 (2009) 554-559.
    [10] Q. Liu, Y. Li, J. Zhang, Y. Chi, X. Ruan, J. Liu, G. Qian, Effective removal of zinc from aqueous solution by hydrocalumite, Chemical Engineering Journal, 175 (2011) 33-38.
    [11] M. Al-Rashed, J. Wójcik, R. Plewik, P. Synowiec, A. Kuś, Multiphase CFD modeling: Fluid dynamics aspects in scale-up of a fluidized-bed crystallizer, Chemical Engineering and Processing: Process Intensification, 63 (2013) 7-15.
    [12] P. Zhou, J.-C. Huang, A.W.F. Li, S. Wei, Heavy metal removal from wastewater in fluidized bed reactor, Water Research, 33 (1999) 1918-1924.
    [13] L.K. Wang, Y.-T. Hung, N. K.Shammas, Physicochemical Treatment Process, Humana Press, USA, 2005.
    [14] G. Falk, C. Litz, R. Taylor, Wastewater Technology Fact Sheet: Chemical Precipitation, in, United States Environment Protection Agency, Washington D.C., USA, 2000.
    [15] J.W. Patterson, H.E. Allen, J.J. Scala, Carbonate Precipitation for Heavy Metals Pollutants, Journal (Water Pollution Control Federation), 49 (1977) 2397-2410.
    [16] M.S. Oncel, A. Muhcu, E. Demirbas, M. Kobya, A comparative study of chemical precipitation and electrocoagulation for treatment of coal acid drainage wastewater, Journal of Environmental Chemical Engineering, 1 (2013) 989-995.
    [17] C.Y. Tai, W.C. Chien, C.Y. Chen, Crystal growth kinetics of calcite in a dense fluidized-bed crystallizer, AIChE Journal, 45 (1999) 1605-1614.
    [18] O. Levenspiel, Chemical Reaction Engineering, Wiley, New York, USA, 1972.
    [19] J.J.M. Werner Stumm, Aquatic Chemistry, John Wiley and Sons Inc., New York, USA, 1996.
    [20] B.J. Alloway, Heavy Metals in Soils: Trace Metals and Metalloids in Soils and their Bioavailability, Springer, United Kingdom, 2012.
    [21] L.G. Gibilaro, Fluidization Dynamics, 1 ed., Butterworth-Heinemann, England, 2001.
    [22] D. Kunii, O. Levenspiel, Fluidization Enginering, 2 ed., Reed Publishing Inc, USA, 1991.
    [23] D.W. Green, R.H. Perry, Perry's Chemical Engineering Handbook, 8 ed., McGraw-Hill Companies Inc, USA, 2008.
    [24] A.S. Myerson, Handbook of Industrial Crystallization, Butterworth-Heinemann New York, USA, 1993.
    [25] A.G. Jones, Crystallization Process Systems, Butterworth-Heinemann, London, UK, 2002.
    [26] R. Aldaco, A. Garea, A. Irabien, Fluoride Recovery in a Fluidized Bed:  Crystallization of Calcium Fluoride on Silica Sand, Industrial & Engineering Chemistry Research, 45 (2005) 796-802.
    [27] F. Mathew, Removal of Heavy Metals from Electroplating Wastewater Using Rice Husk and Coconut Coir, in: Chemical Engineering Department, Missouri University of Science and Technology, USA, 2008, pp. 89.
    [28] D. Kashchiev, Nucleation: Basic Theory with Applications, Butterworth-Heinemann, Oxford, Great Britain, 2003.
    [29] J.P. Chen, Decontamination of Heavy Metals: Processes, Mechanism, and Application, CRC Press, NW, United States, 2012.
    [30] J. L.Wray, F. Daniels, Precipitation of Calcite and Aragonite, Journal of The American Chemical Society, 79 (1957) 2031-2034.
    [31] E. Tsotas, A. S.Mujumdar, Modern Drying Technology, Wiley-VCH, Weinheim, Germany, 2012.

    [32] R. David, P. Marchal, J.-P. Klein, J. Villermaux, Crystallization and precipitation engineering—III. A discrete formulation of the agglomeration rate of crystals in a crystallization process, Chemical Engineering Science, 46 (1991) 205-213.
    [33] T.P. Melia, Crystal nucleation from aqueous solution, Journal of Applied Chemistry, 15 (1965) 345-357.
    [34] C.B. Richardson, T.D. Snyder, A Study of Heterogeneous Nucleation in Aqueous Solution, Langmuir, 10 (1994) 2462 - 2465.
    [35] R. David, P. Marchal, B. Marcant, Modelling of agglomeration in industrial crystallization from solution, Chemical Engineering & Technology, 18 (1995) 302-309.
    [36] P. Ghosh, A.N. Samanta, S. Ray, Reduction of COD and removal of Zn2+ from rayon industry wastewater by combined electro-Fenton treatment and chemical precipitation, Desalination, 266 (2011) 213-217.

    無法下載圖示 校內:2017-08-04公開
    校外:不公開
    電子論文尚未授權公開,紙本請查館藏目錄
    QR CODE