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  1. NTU Theses and Dissertations Repository
  2. 生物資源暨農學院
  3. 生物機電工程學系
請用此 Handle URI 來引用此文件: http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/36346
完整後設資料紀錄
DC 欄位值語言
dc.contributor.advisor吳中興(Chung-Hsing Wu)
dc.contributor.authorKai-Yuan Yangen
dc.contributor.author楊凱元zh_TW
dc.date.accessioned2021-06-13T07:57:45Z-
dc.date.available2006-07-26
dc.date.copyright2005-07-26
dc.date.issued2005
dc.date.submitted2005-07-23
dc.identifier.citation[1]. Andrea, P. O., D. S. Itamar, J. M. Genesio and D. S. Rogerio Jose, 1998. “Efficiency of destruction of waste used in the co-incineration in the rotary kilns”. Energy Conversion Management. Vol. 39, pp. 1899-1909.
[2]. Caretto, L.S., A.D. Gosman, S.V. Patankar and D.B. Spalding, 1972. “Two calculation procedures for steady, three-dimensional flows with recirculation”. Proc. 3rd. Int'l Conference on Numerical Methods for Fluid Mechanics. Lecture Notes on Physics, Springer-Verlag: New York. Vol. 19, pp. 60-68.
[3]. Chen, K. S. and M. Lee, 1995. “Visualization studies of three dimensional flow and solid motion in a rotary kiln”. Hazardous waste and hazardous materials. Vol. 12, No. 4, pp. 395-409.
[4]. Cheng, D.Y. and W.H. Zheng, 1992. Introduction to Industrial Kiln Operation. Xu’s Foundation
[5]. Cundy, V. A. and C. A. Cook, 1996. “Three dimensional numerical modeling of a field-scale rotary kiln incinerator”. Environmental Science and Technology.
[6]. El-Banhawy, Y.H., Siv-Asegaram, S. 1983. “Premixed, turbulent combustion of a sudden-expansion flow”. Combustion and Flame. Vol. 80, pp 153-165.
[7]. Feng, M., J. Goodenough, K. Huang and C. Milliken. 1996. Journal of Power Sources. Vol. 64. pp.47.
[8]. Irvine, J.T.S. and A. Sauve. 2001. “Improved oxidation of hydrocarbons with new electrodes in high temperature fuel cell”. Fuel Cells. 1(34), pp. 205-210.
[9]. Ishihara, T., H. Matsuda and Y. Takita.1994. “Doped LaGaO3 perovskite type oxide as a new oxide ionic conductor”. Journal of the American Chemical Society. 116 (9). pp. 3801-3803
[10]. James, L. and D. Andrew. 2003. Fuel Cell System Explained. John Wiley & Sons. pp. 207-226.
[11]. Khan, J. A., D. Pal and J. S. Morse, 1993. “Numerical modeling of a rotary kiln incinerator”. Hazardous Waste and Hazardous Materials. Vol. 10, pp. 81-95.
[12]. Kramker, F. A. and J. B. Wilson, 1986. “Computer simulation of a rotary dryer Part II: Heat and Mass Transfer”. AIChE. Vol. 32, No. 2, pp. 269-275.
[13]. Lewis, M. H. and L. D. Smoot, 1982 “Turbulent gaseous combustion and flame”. Vol. 42, pp. 183-196.
[14]. Linak, W. P., J. D. Kilgroe and J. E. Mcsorley, 1987. “On the occurrence of transient puffs in a rotary kiln incineration simulator I. Prototype Solid Plastic Wastes”. JAPCA Journal. Vol. 37, pp. 54-64.
[15]. Magnussen, B.F. and B.H. Hjertager, 1976. “On mathematical modeling of turbulent combustion with special emphasis on soot formation and combustion”. Sixteenth International Symposium on Combustion. The Combustion Institute, pp 719-729.
[16]. Mastorakos, E. et al., 1999. “CFD prediction for cement kilns including flame modeling, heat transfer and clinker chemistry”. Applied Mathematical Modeling. Vol. 23, pp. 55-76.
[17]. Patankar, S.V. and D.B. Spalding, 1972. “A calculation procedure for heat, mass, and momentum transfer in three-dimensional parabolic flows”. International J. Heat Mass Transfer. Vol. 15, pp. 1787-1806.
[18]. Perry, M.E., T. Tsai and S.A. Barnett. 1999. “A direct methane fuel cell with ceria-based anode”. Nature. 400, pp. 649-651.
[19]. Pershing, D. W., J. S. Lighty, G. D. Silcox, M. P. Heap and W. D. Owens, 1993. “Solid waste incineration in rotary kilns”. Combustion Science and Technology. Vol. 93, pp. 245-276.
[20]. Silcox, G. D., F. S. Larsen and D. W. Pershing, 1990. “Mathematical and physical modeling of rotary kilns with application to scaling and design”. Incineration of Hazardous Waste and Toxic Combustion By-products.
[21]. Spalding, D.B. 1971. “Mixing and chemical reaction in steady confined turbulent flames”. 13th International Symposium on Combustion—The Combustion Institute. pp. 649-657.
[22]. Thurnau, R. C. and J. A. Manning, 1995. “Low temperature desorption application of a derect-fired rotary kiln incinerator”. Journal of Air and Waste Manage Association. Vol. 46, pp. 12-19.
[23]. Veranth, J. M., G. D. Silcox and D. W. Pershing, 1997. “Numerical modeling of the temperature distribution in a commercial hazardous waste slagging rotary kiln”. Environmental Science and Technology. Vol. 31, pp. 2534-2539.
[24]. Versteeg, H.K. and W. Malalasekera, 1995. An Introduction to Computational Fluid Dynamics, the Finite Volume Method. Addison Wesley Longman: England. pp. 100-102.
[24]. Walter, H. D., Cement-Data-Book. 1976. Bauverlag GmbH Wiesbaden und Berlin. p.336
[25]. Wu, C.H., Z.W. Wu, S.Z. Su, H.P. Lin and Z.Y. Dai. 1996. Integrated Research of Waste Incineration. Technical Report of National Science Council. Vol. 1, pp. 78-81.
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/36346-
dc.description.abstract本文提出一全新的技術觀念:利用目前現存之旋轉窯熱流場提供固態氧化燃料電池(SOLID OXIDE FUEL CELL, SOFC)所需之高溫操作環境。現今的新型管式SOFC設計 (TSOFC) 更適合於旋轉窯之安裝與操作,為數種燃料電池中最為適與汽電共生或與焚化爐結合的類型。
故本文以其為研究對象,合理地假設並評估其安裝的可行性,並發現妥善安排的燃料電池模組共可產出達39.59MW的電能。
本實驗並採用計算流體力學軟體FLUENT之有限體積分析法解工業用旋轉窯焚化爐窯體內之熱流場、向量場、與物質反應的偏微分方程式,以反應操作模式中燃燒所需之過剩空氣量與溫度、旋轉爐之旋轉速度為主要參數,模擬燃燒氣體熱流場與旋轉窯壁之熱傳模式。模擬結果與實際現場量測所得之溫度數值作相互比對,以進行各不同之燃燒反應參數在流場顯影之探討,最後並依照其燃燒熱流場及窯壁內部溫度之分佈預測,進行固態氧化物燃料電池於旋轉窯爐床安裝之可行性探討。
zh_TW
dc.description.abstractWhen meeting the shortage of fossil fuels and the coming era of hydrogen energy, fuel cell energy emerged to be a promising technology in energy utilization in the future.
Developed to work at 800 to 1,000 degree Celsiusand and up to 15 atm (tested by Ontario Hydro Technology), solid oxide fuel cells (SOFCs) can generate the maximum power output among all types of fuel cells. However, when operating the SOFCs, great amount of fossil fuel is actually consumed in order to meet their high-temperature demand. High amount of secondary pollutants are expelled accordingly.
A possible brand new idea is thus proposed in this paper—a state-of-the-art tubular SOFC (TSOFC) can be installed either in the three dimensional heat flow field inside the cement industrial rotary kiln incinerator (RKI, located in Kaohsiung, Taiwan) or within its refractory layer where high temperature environment sustains around the clock when operating for the cement production. In this paper, simulation of the heat flow field and species remained after combustion in this kiln incinerator is achieved with the help of modern computer aided engineering (CAE) tool.
Suitable manipulating regions are to be found and predicted via the commercially available CFD code FLUENT. Parameter of excess air values are the primary variable, the detailed interior heat flow field and the heat transfer model in the kiln shell are the secondary variables for evaluating the installation of SOFCs into rotary kilns.
Before going on this study, kinetic parameters are parametrically varied and finite volume method (FVM) is introduced to solve the heat flow field and the visualization of the three dimensional flame structure is performed. Meanwhile, simulation of temperature results is compared with on-site field experiments and the installation possibilities of the SOFC on the rotary kiln incinerator can be reasonably predicted and assured
en
dc.description.provenanceMade available in DSpace on 2021-06-13T07:57:45Z (GMT). No. of bitstreams: 1
ntu-94-R91631029-1.pdf: 1224775 bytes, checksum: 8f99f380197876f888615ee92e9909e6 (MD5)
Previous issue date: 2005
en
dc.description.tableofcontentsAbstract in Chinese------------------------------------------------------------1
Abstract in English------------------------------------------------------------2
Nomenclature-------------------------------------------------------------------3
Table of Contents--------------------------------------------------------------5
List of Figures ----------------------------------------------------------------7
List of Tables --------------------------------------------------------------------9
Chapter 1 Introduction-----------------------------------------10
Chapter 2 Literature Review-----------------------------------------11
Chapter 3 Physical Descriptions-------------------------------------13
3.1. Solid Oxide Fuel Cell-----------------------------------------------13
3.2. Cement Industry----------------------------------------------------17
3.2.1. Rotary Kiln-------------------------------------------------------17
3.2.2. Cement Formation Process------------------------------------18
3.2.3. Combustion Fuels of the Rotary Kiln-------------------------19
Chapter 4 Results and Discussions------------------23
4.1. Numerical Approach of the Kiln Incinerator----------------23
4.2. Installation Possibility inside the Furnace Body-----------28
4.3. Installation Possibility inside the Refractory Layer around the Kiln Shell-----30
4.4. Power Estimation and Possible Strategy for Installing SOFC Stacks-----33
Chapter 5 Conclusion Remarks--------------------------------36
References-------------------------------------------------------37
Appendix -------------------------------------------------------------40
Author Resume-----------------------------------------------------50
dc.language.isoen
dc.subject有限體積法 (FVM)zh_TW
dc.subject廢熱回收zh_TW
dc.subject固態氧化燃料電池(SOFC)zh_TW
dc.subject旋轉窯 (RKI)zh_TW
dc.subject電腦輔助工程(CAE)zh_TW
dc.subject計算流體力學 (CFD)zh_TW
dc.subjectFLUENTzh_TW
dc.subjectfinite volume method (FVM)en
dc.subjectsolid oxide fuel cell (SOFC)en
dc.subjectFLUENTen
dc.subjectcomputational fluid dynamics (CFD)en
dc.subjectcomputer-aided engineering (CAE)en
dc.subjectrotary kiln incinerator (RKI)en
dc.subjectwaste heat managementen
dc.title逆流式水泥旋轉窯三維燃燒流場之廢熱回收於燃料電池之應用可能性分析zh_TW
dc.titlePredictive Application of Retrievable Waste Heat of the Cement Industrial Rotary Kiln on Solid Oxide Fuel Cellsen
dc.typeThesis
dc.date.schoolyear93-2
dc.description.degree碩士
dc.contributor.oralexamcommittee陳石法(Shi-Fa Chen),黃勝銘(Sheng-Ming Huang),陳康興(Kang-Hsin Chen),戴志揚(Zhi-Yang Dai)
dc.subject.keyword廢熱回收,固態氧化燃料電池(SOFC),旋轉窯 (RKI),電腦輔助工程(CAE),計算流體力學 (CFD),FLUENT,有限體積法 (FVM),zh_TW
dc.subject.keywordwaste heat management,solid oxide fuel cell (SOFC),rotary kiln incinerator (RKI),computer-aided engineering (CAE),computational fluid dynamics (CFD),FLUENT,finite volume method (FVM),en
dc.relation.page50
dc.rights.note有償授權
dc.date.accepted2005-07-24
dc.contributor.author-college生物資源暨農學院zh_TW
dc.contributor.author-dept生物產業機電工程學研究所zh_TW
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