博碩士論文 93323054 詳細資訊




以作者查詢圖書館館藏 以作者查詢臺灣博碩士 以作者查詢全國書目 勘誤回報 、線上人數:48 、訪客IP:18.116.88.118
姓名 劉建嘉(Chien-Chia Liu)  查詢紙本館藏   畢業系所 機械工程學系
論文名稱 利用高速高解析數位質點影像測速儀定量量測Taylor-Couette流場之無特徵紊流
(A study on featureless turbulence of Taylor-Couette flow using high speed, high resolution particle image velocimetry)
相關論文
★ 蚶線形滑轉板轉子引擎設計與實作★ 實驗分析預混紊焰表面密度傳輸方程式及Bray-Moss-Libby模式
★ 低紊流強度預混焰之傳播及高紊流強度預混焰之熄滅★ 預混火焰與尾流交相干涉之實驗研究
★ 自由傳播預混焰與紊流尾流交互作用﹔火焰拉伸率和燃燒速率之量測★ 重粒子於泰勒庫頁提流場之偏好濃度與下沈速度實驗研究
★ 潔淨能源:高效率天然氣加氫燃燒技術與污染排放物定量量測★ 預混焰與紊流尾流交互作用時非定常應變率、曲率和膨脹率之定量量測
★ 實驗方式產生之均勻等向性紊流場及其於兩相流之應用★ 液態紊流噴流動能消散率場與微尺度間歇性 之定量量測
★ 預混焰和紊流尾流交互作用:拉伸率與輻射熱損失效應量測★ 四維質點影像測速技術與微尺度紊流定量量測
★ 潔淨能源:超焓燃燒器研發★ 小型熱再循環觸媒燃燒器之實驗研究及應用
★ 預混紊流燃燒:碎形特性、當量比 和輻射熱損失效應★ 預混甲烷紊焰拉伸量測,應用高速PIV
檔案 [Endnote RIS 格式]    [Bibtex 格式]    [相關文章]   [文章引用]   [完整記錄]   [館藏目錄]   [檢視]  [下載]
  1. 本電子論文使用權限為同意立即開放。
  2. 已達開放權限電子全文僅授權使用者為學術研究之目的,進行個人非營利性質之檢索、閱讀、列印。
  3. 請遵守中華民國著作權法之相關規定,切勿任意重製、散佈、改作、轉貼、播送,以免觸法。

摘要(中) 本研究利用數位質點影像測速儀(digital particle image velocimetry,DPIV)與小波轉換(wavelet transform),針對著名的Taylor-Couette (TC)流場中尚未被詳細探討的無特徵紊流(featureless turbulence),首度定量量測分析其重要的時間與空間尺度及頻譜特性。無特徵紊流乃由兩同軸內外長圓柱於特定轉速下反向旋轉而得,經Andereck et al. (1986)液態流場觀測發現沒有比內外圓柱間隙尺度更大的特徵結構存在,故稱之為無特徵紊流。Ronney團隊(1995)由雷射都普勒測速量儀(laser Doppler velocimetry,LDV)得知,液態無特徵紊流之平均速度近似零並且具有相當均勻的空間特性。本實驗首度進行氣態無特徵紊流之DPIV量測,擷取氣態流場之軸向、徑向和切線方向之時序與空間速度資訊,接著利用小波轉換分解速度尺度,進一步獲得流場之尺度、能量頻譜與間歇性特性。本研究回答下列三個問題:(1)如何辨識無特徵紊流?(2)無特徵紊流之能量生成與消散之關鍵的時空特徵尺度為何?(3)固態重粒子(密度遠大於流體)在無特徵紊流中的下沉機制為何?我們發現無特徵紊流三個維度之速度分量,其平均速度相對於其紊流強度皆可被忽略,且其瞬時速度之機率密度函數皆呈高斯分布,此氣態流場結果與Ronney團隊液態流場結果相符。任一維度之能量頻譜在慣性區(inertial range)內的遞減斜率皆呈-5/3,顯示無特徵紊流具有全展紊流(fully-developed turbulence)的基本特性。間歇性會隨著渦漩尺度變小而增強,證實無特徵紊流具有活躍的小尺度活動,且由小波分析所得之間歇性最強的尺度大小與傳統紊流理論公式所估算之最小尺度值其量級(order of magnitude)相符。在二相紊流研究中,我們採用同一條件之無特徵紊流場,搭配平均粒徑為40與60 ?m的玻璃重粒子,其Rep = VtDp/?皆小於1,故在自由落下之過程仍受線性阻力,待其達終端速度後才進入無特徵紊流場,其中Vt、Dp和?分別是重粒子之終端速度、粒徑以及流體之運動黏滯係數。相對應之Stokes數(St = ?p/?K,其中?p和?K分別是重粒子達終端速度所需的時間與流場之Kolmogorov時間尺度)為6或13的玻璃重粒子,其下沉軌跡深受流場內反向對轉之非定常渦漩對的影響,會沿著渦漩周圍呈現加速、減速或形成水平運動。重粒子之下沉速度,最高甚至可達終端速度的兩倍以上,其增幅約為流場均方根紊流強度的一半。
摘要(英) This study aims to measure and analyze important spatiotemporal characteristics of featureless turbulence of the well-known Taylor-Couette (TC) flow using high-speed, high-resolution digital particle image velocimetry (DPIV) and wavelet analyses. Featureless turbulence is generated by two concentric counter-rotating, at some specific rotating speeds, inner and outer long cylinders. Andereck et al. (1986) via liquid flow visualization had first noticed that no dominant large structures being larger than the annulus gap width can be observed, so they named it featureless turbulence. Ronney et al. (1995) showed that this liquid flow is nearly homogeneous across the annulus with the negligible mean velocity by laser Doppler velocimetry (LDV). DPIV measurement of gaseous featureless turbulence was first conducted here, and the radial, axial and azimuthal velocity data of this flow were acquired. By decomposing the obtained spatiotemporal velocity data by wavelet transform, the subsequent scale, energy spectrum and intermittency analyses were obtained for the analyses. Focuses are placed on the following three goals. (1) By what means can featureless turbulence be recognized? (2) What are the characteristic spatiotemporal scales relevant to energy production and dissipation of featureless turbulence? (3) Does the preferential sweeping exist for the particle settling? We found that every velocity component is of a near-Gaussian distribution with the negligible mean velocity comparative to its turbulence intensity everywhere in the flow, so that this flow is near homogeneous, consistent with the previous result (Ronney et al. 1995). Energy spectra showed a -5/3 decaying slope in the inertial subrange, proving the essential factor of fully-developed turbulence. Intermittency level was found to increase as the eddy scale decreases, validating existence of the violent small scale motion. The highest intermittency showed up at the same order of magnitude of the estimated smallest scale. In two-phase study, the settling phenomenon of heavy glass particles was observed. The glass particles that were subject to a linear drag force (Rep = VtDp/? < 1, where Vt, Dp and ? are the terminal velocity and the diameter of the heavy particle, and the kinematic viscosity of the fluid), St ≈ 6 or 13 (St = ?p/?K, where ?p and ?K are respectively the particle relaxation time and the Kolmogorov time scale), were found to response well to vortex structures in featureless turbulence, and showed a preferential sweeping along down flow side of the periphery of the strong vortex structure. An apparent change in motion of the particle due to the strong vortex pairing was observed, and in some cases the particle appeared in horizontal movement, but others the particle settling rate could be twice as the original value, about half of the turbulence intensity in raise.
關鍵字(中) ★ 無特徵紊流
★ 數位質點影像測速儀
★ 小波轉換
★ Taylor-Couette流場
關鍵字(英) ★ Digital Particle Image Velocimetry
★ Taylor-Couette Flow
★ Featureless Turbulence
★ Wavelet Analysis
論文目次 Chapter 1 Introduction 1
1-1 Motivation 1
1-2 Unsolved Problems 2
1-3 Thesis Outline 2
Chapter 2 Literature Review 3
2-1 Taylor-Couette Flow 3
2-2 Featureless Turbulence 4
2-3 Isotropic Turbulence 6
2-4 Energy Cascade 6
2-5 Two-Phase Flow 8
2-6 Preferential Sweeping in Two-Phase Flow 9
Chapter 3 Experimental Apparatus and Diagnostics 10
3-1 Apparatus and Operating Conditions 10
3-2 Diagnostics 11
3-2-1 Digital Particle Image Velocimetry 11
3-2-2 Vorticity and Strain Rate 12
3-2-3 Wavelet-Based Analysis 13
Chapter 4 Results and Discussion 15
4-1 Featureless Turbulence 15
4-2 Experimental Uncertainties 17
4-2 Vortex pair 19
4-3 Scale Analysis 19
4-4 Energy Spectra and Intermittency 20
4-5 Preferential Sweeping in Two-Phase Flow 22
Chapter 5 Conclusions and Future Work 25
5-1 Conclusions 25
5-2 Future Work 25
References 27
參考文獻 Abdel-Gayed, R. G., Bradley, D. & Lawes, M. 1987 Turbulent burning velocities: A general correlation in terms of straining rates. Proc. R. Soc. Lond. A 414, 389-413.
Akonur, A. & Lueptow, R. M. 2003 Three-dimensional velocity field for wavy Taylor-Couette flow. Phys. Fluids 15, 947-960.
Aldredge, R. C. 1996 A novel flow reactor for the study of heat-loss effects on turbulent flame propagation. Int. Comm. Heat Mass Trans. 23, 1173-1179.
Aldredge, R. C., Vaezi, V. & Ronney, P. D. 1998 Premixed-flame propagation in turbulent Taylor-Couette flow. Combust. Flame 115, 395-405.
Andereck, C. D., Liu, S. S. & Swinney, H. L. 1986 Flow regimes in a circular Couette system with independently rotating cylinders. J. Fluid Mech. 164, 155-183.
Coles, D. 1965 Transition in circular Couette flow. J. Fluid Mech. 21, 385-425.
Durbin, P. A. & Petterson Reif, B. A. 2001 Statistical theory and modeling for turbulent flows. John Wiley & Sons.
Fenstermacher, P. R., Swinney, H. L. & Gollub, J. P. 1979 Dynamical instabilities and the transition to chaotic Taylor vortex flow. J. Fluid Mech. 94, 103-128.
Frisch, U. 1995 Turbulence: The legacy of A.N. Kolmogorov. Cambridge University Press.
Goharzadeh, A. & Mutabazi, I. 2001 Experimental characterization of intermittency regimes in the Couette-Taylor system. Eur. Phys. J. B 19, 157-162.
Gollub, J. P. & Swinney, H. L. 1975 Onset of turbulence in a rotating fluid. Phys. Rev. Lett. 35, 927-930.
Hinze, J. O. 1959 Turbulence. McGraw-Hill.
Mathieu, J. & Scott, J. 2000 An introduction to turbulent flow. Cambridge University Press.
Maxey, M. R. 1987 The gravitational settling of aerosol particles in homogeneous turbulence and random flow fields. J. Fluid Mech. 174, 441-465.
Robinson, A. L. 1983 How does fluid flow become turbulent? Science 221, 140-143.
Ronney, P. D., Haslam, B. D. & Rhys, N. O. 1995 Front propagation rates in randomly stirred media. Phys. Rev. Lett. 74, 3804-3807.
Saffman, P. G. 1992 Vortex dynamics. Cambridge University Press.
Taylor, G. I. 1923 Stability of a viscous liquid contained between two rotating cylinders. Phil. Trans. R. Soc. Lond. A 223, 289-343.
Tennekes, H. & Lumley, J. L. 1972 A first course in turbulence. MIT Press.
Tritton, D. J. 1977 Physical fluid dynamics. Van Nostrand Reinhold.
Vaezi, V., Oh, E. S. & Aldredge, R. C. 1997 High-intensity turbulence measurements in a Taylor-Couette flow reactor. Exp. Thermal Fluid Sci. 15, 424-431.
Weisberg, A. Y., Kevrekidis, I. G. & Smits, A. J. 1997 Delaying transition in
Taylor-Couette flow with axial motion of the inner cylinder. J. Fluid Mech. 348, 141-151.
Wereley, S. T. & Lueptow, R. M. 1998 Spatio-temporal character of non-wavy and wavy Taylor-Couette flow. J. Fluid Mech. 364, 59-80.
Wereley, S. T. & Lueptow, R. M. 1999 Velocity field for Taylor-Couette flow with an axial flow. Phys. Fluids 11, 3637-3649.
Yang, C. Y. & Lei, U. 1998 The role of the turbulent scales in the settling velocity of heavy particles in homogeneous isotropic turbulence. J. Fluid Mech. 371, 179-205.
Yang, T. S. & Shy, S. S. 2003 The settling velocity of heavy particles in an aqueous near-isotropic turbulence. Phys. Fluids 15, 868-880.
Yang, T. S. & Shy, S. S. 2005 Two-way interaction between solid particles and air turbulence: particle settling rate and turbulence modification measurements. J. Fluid Mech. 526, 171-216.
Yang, T. S., Shy, S. S. & Chyou, Y. P. 2005 Spatiotemporal intermittency measurements in a gas-phase near-isotropic turbulence using high speed DPIV and wavelet analysis. J. Mech. 21, 157-169.
指導教授 施聖洋(Shenqyang (Steven) Shy) 審核日期 2006-7-24
推文 facebook   plurk   twitter   funp   google   live   udn   HD   myshare   reddit   netvibes   friend   youpush   delicious   baidu   
網路書籤 Google bookmarks   del.icio.us   hemidemi   myshare   

若有論文相關問題,請聯絡國立中央大學圖書館推廣服務組 TEL:(03)422-7151轉57407,或E-mail聯絡  - 隱私權政策聲明