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http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/49045完整後設資料紀錄
| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 陳誠亮 | |
| dc.contributor.author | Po-Yi Li | en |
| dc.contributor.author | 李柏毅 | zh_TW |
| dc.date.accessioned | 2021-06-15T11:14:31Z | - |
| dc.date.available | 2016-08-25 | |
| dc.date.copyright | 2016-08-25 | |
| dc.date.issued | 2016 | |
| dc.date.submitted | 2016-08-20 | |
| dc.identifier.citation | [1] Aspen Technology, Inc. Aspen Energy AnalyzerTutorial Guide. Aspen Tech-nology, Inc., 1988.
[2] Brooke, A., Kendrick. D., Meeraus, A., Raman, R., and Rosenthal, R. E. GAMS: A User’s Guide. GAMS Development Corporation, 1988. [3] Chen, C.L., Chang F.Y., Chao T,H., Chen H.C. and Lee J.Y. ”Heat-exchanger network synthesis involving organic Rankine cycle for waste heat recovery”. Ind. Eng. Chem. Res., 53(44):16924–36, 2014. [4] Choate, W. T., and Ilona, J. ”Waste Heat Recovery: Technology and Oppor¬tunities in U.S. Industry.”. Technical report, U.S. DOE, 2008. [5] Colberg, R. D., and Morari, M. ”Area and capital cost targets for heat ex¬changer network synthesis with constrained matches and unequal heat transfer coefficients.”. Comput. Chem. Eng., 14(1):1, 1990. [6] Dai, Y., Wang, J.and Lin, G. ”Parametric optimization and comparative study of organic Rankine cycle (ORC) for low grade waste heat recovery”. Energy Conversion and Management, 50:576–82, 2007. [7] Desai, N. B., and Bandyopadhyay, S. ”Process integration of organic rankine cycle.”. Energy, 34:1674, 2009. [8] Hipolito-Valencia, B. J., Rubio-Castro, E., Ponce-Ortega, J. M., Serna-Gonzalez, M., Napoles-Rivera, F., and EI-Halwagi, M. M. ”Optimal integra¬tion of organic rankine cycles with industrial process.”. Energy Conversion and Management, 73:285, 2013. [9] Hung, T.C., Shai, T. Y.,Wang, S. K., and Tsai, K. F. ”A review of organic Rankine cycles (ORCs) for the recovery of low-grade waste heat.”. Energy, 22(7):661–7, 1997. [10] Hung, T.C., Wang, S. K., Kuo, C. H., Pei, B. S., and Tsai, K. F. ”A study of organic working fluids on system efficiency of an ORC using low grade energy sources.”. Energy, 35:1403, 2010. [11] Obernberger, I., Thonhofer, P. and Reisenhofer, E. ”Description and evalu¬ation of the new 1000 kW organic Rankine cycle process integrated in the biomass CHP plant in Lienz, Austria”. Euroheat and Power, 10:661–7, 2002.75 [12] Perry, R.H., Green D.W., Maloney J.O., editor. Perry’s Chemical Engineers’ Handbook. McGraw-Hill, 1997. [13] Raman, R., and Grossmann, I. E. ”Modeling and computational techniques for logic based integer programming.”. Comput. Chem. Eng., 18:563, 1994. [14] Smith.R. Chemical Process Design and Integration. Wiley, 2008. [15] Wei, D., Lu, Xuesheng, Lu Zhen, Gu, L. ”Performance analysis and opti¬mization of organic Rankine cycle (ORC) for waste heat recovery”. Energy Conversion and Management, 48(4):1113–19, 2007. [16] Yee, T. F., and Grossmann, I. E. ”Simultaneous optimization models for heat integration-II. Heat exchanger network synthesis.”. Comput. Chem. Eng., 14:1165, 1990b. [17] Yee, T. F., Grossmann, I. E., and Kravanja, Z. ”Simultaneous optimization models for heat integration-I. Area and energy targeting and modeling of multi-stream exchangers.”. Comput. Chem. Eng., 14:1151, 1990a. | |
| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/49045 | - |
| dc.description.abstract | 有機朗肯循環是一種將熱轉換為功的循環，其中使用低沸點的有機流體作為工作流體。廢熱回收是有機朗肯循環最重要的發展領域之一，它可以被應用在發電廠會是工廠等程序。某些熱源會含有粒子與硫化物可能會對蒸發器的管線產生損害，例如熱爐產生的廢氣。會建議利用水或是熱傳油來當作中間的循環流體，間接取熱。在這篇論文中，發表了一個整合有機朗肯循環與熱傳油來從其他程序回收廢熱的數學模型，整合有機朗肯循環的超結構考慮了所有在程序熱流、循環熱傳油及有機朗肯循環之間的熱交換器配對可能性。藉由這個超結構，發展出混合整數非線性規劃的模型。我們利用高階的模型程式GAMS來求此混合整數非線性規劃模型的解。以一個原油分餾工廠來當作案例，進行模擬及後續的結果討論，另外也採用回收年限法來評估其經濟效應。 | zh_TW |
| dc.description.abstract | An organic Rankine cycle (ORC) uses a low boiling point organic fluid as a working medium. Waste heat recovery is one of the most important development fields for the organic Rankine cycle (ORC).It can be applied to heat and power plants, or to industrial and farming processes. Some heat sources ,like hot exhausts from furnaces,which contains particles or sulfide might hurt pipes of evaporator.It is suggested to introduce water or heat transfer oil as an intermediate medium.In this paper, a mathematical model is presented for integrate ORC with the heat transfer oil recirculated as a intermediate fluid for recovering waste heat from the background process.A ORC-integrated superstructure considering all possible match of heat-exchange between process hot streams, recirculating hot oil and ORC is proposed.The possibility of several sets of ORC and recirculating hot oil also be concerned in the superstructure.On the basis of this superstructure, the model is formulated as a mixed-integer nonlinear program (MINLP).This MINLP model is designed and solved by a high-level modeling system, General Algebraic Modeling System (GAMS).A case about crude pre-heat train is solved to demonstrate the application of the proposed model for industrial waste heat recovery.Payback year method is applied to evaluate the cost of the additional capital equipment. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-15T11:14:31Z (GMT). No. of bitstreams: 1 ntu-105-R02524079-1.pdf: 2237914 bytes, checksum: 0adeda0fc1ef96ba7c7a380e5b157cea (MD5) Previous issue date: 2016 | en |
| dc.description.tableofcontents | 目 錄
誌謝……………………………………………………………………………………………………… i 摘要……………………………………………………………………………………………………… iii Abstract…………………………………………………………………………………………… v 附圖目錄……………………………………………………………………………………………… ix 附表目錄……………………………………………………………………………………………… xi 1 緒論 1 1.1 前言…………………………………………………………………………………………… 1 1.2 有機朗肯循環的介紹………………………………………………………… 2 1.3 文獻回顧…………………………………………………………………………………… 6 1.4 研究動機與目的…………………………………………………………………… 7 1.5 組織章節 ………………………………………………………………………………… 11 2. 間接有機朗肯循環模式建構 13 2.1 模式建立之背景說明與想法……………………………………………… 13 2.2 模型建立之基本假設條件…………………………………………………… 14 2.3 模型建立之圖解說明……………………………………………………………… 16 2.4 模型隻符號、集合、系統參數與變數(indices, Sets,Parameter, and Variables)……………………………………… 17 2.5 目標函數與限制式(Objective Function and Contraints)……………………………………………………………………………………………………………………… 21 2.5 限制式(Contraints)…………………………………………………… 21 2.5 目標函數(Objective Function)………………………… 29 2.5 間接有機朗肯循環模型整合………………………………………… 29 3. 模擬結果最適化與討論 31 3.1 模擬結果最適化………………………………………………………………………… 31 3.2 單一程序熱流模擬結果與討論…………………………………………… 32 3.3 原油分餾預熱系統整合單組有機朗肯循環模擬結果與討論.44 3.4 原油分餾預熱系統整合多組有機朗肯循環模擬結果與討論.51 4. 經濟成本評估 55 4.1 經濟評估方法………………………………………………………………………………… 55 4.2 案例結果與討論…………………………………………………………………………… 60 5. 結果與未來展望 67 5.1 結論…………………………………………………………………………………………………… 67 5.2 未來展望………………………………………………………………………………………… 68 附錄 …………………………………………………………………………………………………………………69 參考文獻………………………………………………………………………………………………………… 73 | |
| dc.language.iso | zh-TW | |
| dc.title | 間接有機朗肯循環於化工程序廢熱回收之應用 | zh_TW |
| dc.title | Indirect Organic Rankine Cycle for Waste Heat Recovery in Chemical Processes | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 104-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 錢義隆,吳哲夫,張玨庭,李瑞元 | |
| dc.subject.keyword | 間接取熱,有機朗肯循環,熱傳油,超結構,混合整數非線性規劃,最佳化,回收年限, | zh_TW |
| dc.subject.keyword | indirect,hot transfer oil,organic rankine cycle,Superstructure,Mixed-integer nonlinear programming (MINLP),Optimization, | en |
| dc.relation.page | 74 | |
| dc.identifier.doi | 10.6342/NTU201603339 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2016-08-21 | |
| dc.contributor.author-college | 工學院 | zh_TW |
| dc.contributor.author-dept | 化學工程學研究所 | zh_TW |
| 顯示於系所單位： | 化學工程學系 | |
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