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  1. NTU Theses and Dissertations Repository
  2. 工學院
  3. 化學工程學系
請用此 Handle URI 來引用此文件: http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/67599
完整後設資料紀錄
DC 欄位值語言
dc.contributor.advisor陳誠亮(Cheng-Liang Chen)
dc.contributor.authorYu-Cheng Huangen
dc.contributor.author黃于誠zh_TW
dc.date.accessioned2021-06-17T01:39:34Z-
dc.date.available2022-08-02
dc.date.copyright2017-08-02
dc.date.issued2017
dc.date.submitted2017-07-28
dc.identifier.citation[1] U.S. Energy Information Administration, U.S. Energy Mapping System https://www.eia.gov/state/maps.php?src=home-f3
[2] 台灣中油股份有限公司,天然氣事業部,天然氣輸氣管幹線
http://new.cpc.com.tw/division/lngb/information-text.aspx?id=26
[3] 台北市道路道路管理中心,管線圖查詢
http://dig.nco.taipei/Tpdig3/Default.asp#
[4] Tatsuhiko Kiuchi, An implicit method for transient gas flows in pipe networks., International Journal of Heat and Fluid Flow, October 1994, Vol. 15, No. 5, pp378-383
[5] Mohammad Abbaspour, Kirby S. Chapman, Larry A. Glasgow, Transient modeling of non-isothermal, dispersed two-phase flow in natural gas pipelines, Applied Mathematical Modeling, 2010, 34, pp495-507
[6] E. Benjamin Wylie, Victor L. Streeter, Fluid Transients, FEB Press, Michigan. USA, 1983
[7] E. Bender, Simulation of dynamic gas flows in networks including control loops. Computers & Chemical Engineering, 1979, 3, (1–4), pp611-613.
[8] Poloni, M.; Winterbone, D. E.; Nichols, J. R. In Calculation of pressure and temperature discontinuity in a pipe by the method characteristics and the two-step differential Lax-Wendroff method, American Society of Mechanical Engineers, Fluids Engineering Division (Publication) FED, 1987; pp1-7.
[9] A. E. Fincham, MA, CEng, FIGasE, AFIMA, and M. H. Goldwater, BSc, CEng, MIGasE, Simulation models for gas transmission networks, Transactions of the Institute of Measurement and Control 1979, 1, (1), pp3-13.
[10] Li Changjun, Jia Wenlong and Wu Xia, Modeling and simulation for steady state and transient pipe flow of condensate gas, Thermodynamics - Kinetics of Dynamic Systems, 2011, September, 22, pp65-84
[11] Ning Hsing Chen, An explicit equation for friction factor in pipe, Ind. & Eng. Chem. Fund, 1979, 18(3), pp296-297
[12] Cyril Frank Colebrook, Turbulent Flow in Pipes with Particular reference to the Transition Region between the Smooth and Rough Pipe Laws, J. Inst. of Civil Engrs., 1939, I1, pp 133-156.
[13] Vukalovich, M. P., Aleksandrov, A. A. , Tracgtengerts, M. S., Equations of state for superheated steam for industrial computations using electronic computers. Teploenergetika 1968, 9, pp86-90.
[14] The International Association for the Properties of Water and Steam (IAPWS), http://www.iapws.org/
[15] Bruce Larock, Gary Z. Watters, Roland W. Jeppson, Hydraulics of Pipeline system, CRC Press, Boca Raton, Florida, 2000
[16] McCutcheon, S.C., Martin, J.L, Barnwell, T.O. Jr., Water Quality in Maidment, D.R. (Editor). Handbood of Hydrology, McGraw-Hill, New York, NY , 1993, pp. 11.3
[17] Shiojenn Tseng, Yu-Ming Li, Chih-Yuan Lin, Jyh-Ping Hsu, Salinity gradient power: influences of temperature and nanopore size, Nanoscale, 2016, 8, pp2350-2357
[18] National Institute of Standards and Technology (NIST), Water, Shomate Equation, http://webbook.nist.gov/cgi/cbook.cgi?ID=C7732185&Mask=1
[19] Kishore Sirvole, Transient analysis in pipe netwoks, master thesis, Virginia Polytechnic Institute & State University, 2007, September 25
[20] Adi Ben-Israel, A newton-raphson method for the solution of systems of equations, Journal of Mathematical Analysis and Applications, 1966, 15, pp.243-252
[21] Hardy Cross, Analysis of flow in networks of conduits or conductors. University of Illinois. Engineering Experiment Station. Bulletin,1936; no. 286.
[22] Shih-Han Wang, Wei-Jyun Wang, Chaio-Ying Chang and Cheng-Liang Chen, Analysis of a Looped High Pressure Steam Pipeline Network in a Large-Scale Refinery. Industrial & Engineering Chemistry Research, 2015, 54, (37), pp9222-9229.
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/67599-
dc.description.abstract本研究旨在探討高壓蒸汽網路之動態。首先,確立所需要使用的控制方程式,包含連續方程式、動量守恆方程式以及能量守恆方程式,用這三條控制方程式來求解流速、壓力以及溫度。在數學解析方法中有顯式法和隱式法兩種,顯式法可使用較小的時間間隔,但受限於穩定性且運算時間會拉長;而在隱式法中可使用較長的時間間隔,運算時間也會縮短,且適合用在長時間的動態分析上面。因此在本研究中採用完全隱式法來探討高壓蒸汽網路的動態,另外在求解非線性方程式則是使用牛頓法。
結合完全隱式法和牛頓法,首先運用在可壓縮與不可壓縮流體的單管系統中,運算結果的穩態結果透過和Aspen Plus比較後,確認此運算方法是可行的,之後針對不同的時間間隔和管段間隔進行探討並選出在此運算方法中較適當的數值。之後,在環狀蒸汽網路系統中,利用修正後的哈迪‧克勞斯法來計算蒸汽網路流量分配,並結合進運算迴圈中,模擬的範例包含樹枝狀系統以及三個環狀網路系統,其中包括雙環路系統、多供應端多需求端系統和大型蒸汽網路系統。在不同網路系統中探討,若流量發生變化時,不同的操作方式,會使的各單元有什麼樣的溫度壓力變化,並提供一個參考依據,有助於提高蒸汽網路系統的操作效益。
zh_TW
dc.description.abstractThe purpose of this study is to investigate the transient response analysis of high pressure steam pipeline system. The mathematical model contain three governing equations, included continuity equation, momentum equation and energy equation. With these three governing equations, we can get flow rate, pressure and temperature. There are two types of mathematical analysis method, one is explicit method and the other is implicit method. For explicit method can use smaller time step but time step is limited by stability and computation time will spend more time. For implicit method can be applied to the long-term transients due to it is stable when using large time step and will reduce computation time. Therefore, we use fully implicit method in this study. And the algorithm to solve the governing equations is based on Newton-Raphson method.
Combine fully implicit method and Newton-Raphson method in our calculation loop. In the single pipe system, we simulate two types of fluid, one is compressible fluid and the other is incompressible fluid. Each system is compared with Aspen Plus simulation at steady state. We also discuss different time step and number of sections in order to make a good choice in calculation loop. In the looped steam network, the calculation loop we add modified Hardy Cross method in calculation loop to calculate flow rate distribution. In the case study, start from one special case of looped network: branch network, then we design two-looped network, multi-supply and multi-demand network and larger looped network. In these case studies, transient condition is flow rate change. With different operation, we provide the calculation results of units’ temperature and pressure change. And we hope that we can give them a way to make decision when the transient conditions happen.
en
dc.description.provenanceMade available in DSpace on 2021-06-17T01:39:34Z (GMT). No. of bitstreams: 1
ntu-106-R04524021-1.pdf: 6208121 bytes, checksum: cd8796919d06833d826d09d44e61a9d6 (MD5)
Previous issue date: 2017
en
dc.description.tableofcontents口試委員會審定書 #
致謝 I
中文摘要 II
ABSTRACT III
目錄 IV
圖目錄 VI
表目錄 IX
第一章 緒論 1
1.1 前言 1
1.2 文獻回顧 4
1.3 研究動機 4
1.4 組織架構 5
第二章 蒸汽管網數學模型與解析方法 6
2.1 數學模型之建立 6
2.1.1 基本假設 6
2.1.2 控制方程式 6
2.2 數學解析方法 10
2.2.1 牛頓法 10
2.2.2 完全隱式法 11
2.2.3 運算方法 13
第三章 單管系統分析模擬 15
3.1 有熱傳單管系統 15
3.2 可壓縮流體變化系統 15
3.3 不可壓縮流體變化系統 22
3.4 時間間隔與管段間隔 29
3.4.1 時間間隔(∆t) 30
3.4.2 管段間隔(∆x) 34
第四章 蒸汽網絡系統分析模擬 36
4.1 流體輸送系統 36
4.2 Hardy Cross方法 37
4.3 蒸汽網絡系統 39
4.3.1 蒸汽系統運算流程 39
4.3.2 樹枝狀系統 42
4.3.3 環狀網絡系統範例一 46
4.3.4 環狀網絡系統範例二 49
4.3.5 環狀網絡系統範例三 53
第五章 結論與未來展望 70
5.1 結論 70
5.2 未來展望 71
參考文獻 72
附錄A 75
蒸汽密度表示式 75
蒸汽黏度表示式 76
蒸汽比熱表示式 77
總包熱傳係數表示式 80
水定壓下密度表示式 81
水黏度表示式 81
水比熱表示式 81
水的波速表示式 82
dc.language.isozh-TW
dc.subject蒸汽zh_TW
dc.subject完全隱式法zh_TW
dc.subject牛頓法zh_TW
dc.subject動態分析zh_TW
dc.subject環狀網路系統zh_TW
dc.subjectlooped network systemen
dc.subjectFully implicit methoden
dc.subjectNewton-Raphson methoden
dc.subjecttransient analysisen
dc.subjectSteamen
dc.title高壓蒸汽分配網路之動態分析zh_TW
dc.titleTransient Analysis of High Pressure Steam Distribution Networksen
dc.typeThesis
dc.date.schoolyear105-2
dc.description.degree碩士
dc.contributor.oralexamcommittee錢義隆,吳哲夫,李豪業
dc.subject.keyword蒸汽,完全隱式法,牛頓法,動態分析,環狀網路系統,zh_TW
dc.subject.keywordSteam,Fully implicit method,Newton-Raphson method,transient analysis,looped network system,en
dc.relation.page84
dc.identifier.doi10.6342/NTU201702183
dc.rights.note有償授權
dc.date.accepted2017-07-31
dc.contributor.author-college工學院zh_TW
dc.contributor.author-dept化學工程學研究所zh_TW
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