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http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/42883完整後設資料紀錄
| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 陳誠亮 | |
| dc.contributor.author | Chen-Wei Chang | en |
| dc.contributor.author | 張辰瑋 | zh_TW |
| dc.date.accessioned | 2021-06-15T01:27:25Z | - |
| dc.date.available | 2009-07-29 | |
| dc.date.copyright | 2009-07-29 | |
| dc.date.issued | 2009 | |
| dc.date.submitted | 2009-07-22 | |
| dc.identifier.citation | [1] Rosain RM. Reusing water in CPI plants. Chemical engineering progress 89, 28.
[2] Kim, J., R. Smith. Cooling water system design. Chem. Eng. Sci. 56, 3641 (2001). [3] Wang, Y. and Smith R. Wastewater minimization. Chem. Eng. Sci. 49, 981 (1994). [4] Kim, J., Savulescu. L., R. Smith. Design of cooling system for effluent temperature reduction. Chem. Eng. Sci. 56, 1811 (2001). [5] Kim, J., R. Smith. Automated retrofit design of cooling-water systems. AICHE J.49, 1712 (2003). [6] Feng, X. and Shen B. Wang. Recirculating Cooling-water Network with an intermediate Cooling-Water Main. Energy and Fuels 19, 1723 (2005). [7] C.L.Chen, L.F. Lin, Y.J. Ciou andW.C. Chen. Superstructure-based MINLP formulation for systhesis of re-circulating cooling-water network with intermediate mains. Journal of Chemical Engineering of Japan 40, 235 (2007). [8] Irene Mei Leng Chew, Raymond Tan, Denny Kok Sum Ng, Dominic Chwan Yee Foo. Synthesis of Direct and Indirect Interplant Water Network. Ind. Eng. Chem.Res. 47, 9485 (2008). [9] Jin-Kuk Kim and R. Smith. Cooling system design for water and wastewater minimization.Ind. Eng. Chem. Res. 43, 608 (2004). [10] Gunarantam, M., A.-A. K. A. J.-K. and Smith, R. Automated design of total water systems. Ind. Eng. Chem. Res. 44, 588. [11] S. AHMAD and D. C.W. Htn. Heat recovery between areas of integrity. Computers chem. Engng. 15, 809 (1991). [12] M. AMIDPOUR and G. T. POLLEY. APPLICATION OF PROBLEMDECOMPOSITION IN PROCESS INTEGRATION. Institution of Chemical Engineers 15, 809 (1991). [13] Miguel Bagajewicz and H.Rodera . Energy savings in total site heat integration across many plants. Computers and Chemical Engineering 24, 1237 (2000). [14] S.V. Bedekar, P. Nithiarasu and K.N. Seetharamu. Experimental investigation of the performance of a counter-flow, packed-bed mechanical cooling tower. Energy 23,943 (1998). [15] M.M. Castro, T.W. Song and J.M. Pinto. Minimization of operational costs. Trans IchemE 78, part A (2000). [16] Feng, X. and Seider, W.D. New structure and design methodology for water networks.Ind. Eng. Chem. Res. 40, 6140 (2001). [17] Xiao Feng ., Jie Bai, Huimin Wang, Xuesong Zheng. Grass-roots design of regeneration recycling water networks. Computers and Chemical Engineering 32, 1892 (2008). [18] FENG Xiao, LI Yucai and YU Xinjiang . Improving Energy Performance of Water Allocation Networks. Chinese Journal of Chemical Engineering 16, 480 (2008). [19] Kuo, W., and Smith, R. Effluent treatment system design. Chem. Eng. Sci. 52, 4273 (1997). [20] Kuo, W., and Smith, R. Design of water-using systems involving regeneration, 76, 94 (1998). [21] Liu,Y., Duan, H. and Feng, X. The design of water-reusing network with a hybrid structure through mathematical programming. Chinese Journal of Chemical Engineering 16, 1 (2008). [22] T. Majozi and A. Moodley. Simultaneous targeting and design for cooling water system with multiple cooling water supplies. Computers and Chemical Engineering 32, 540 (2008). [23] M.H. Panjeshahi, A. Ataei, M. Gharaie, R. Parand. Optimum design of cooling water system for energy and water conservation. Chemical Engineering Research and Design 87, 200 (2009). [24] H. Rodera and M.J. Bagajewicz. Targeting procedures for energy saving by heat integration across plants. AIChE 45, 1721 (1999). [25] L.E. Savulescu, M. Sorin and R.Smith. Direct and indirect heat transfer in water network systems. Applied Thermal Engineering 22, 981 (2002). [26] Wang, Y. and Smith, R. Design of distributed effluent treatment system. Chem. Eng. Sci. 49, 3127 (1994). [27] Brooke, A., Kendrick. D., Meeraus, A., Raman, R., and Rosenthal, R. E. GAMS: A User’s Guide (GAMS Development Corporation, 1988). [28] Robin Smith. Chemical Process Design and Integration (Wiley, 2005). [29] Chaplin Tyler, S.M. Chemical Engineering Economics (Mcgraw-Hill Book Company, 1984). | |
| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/42883 | - |
| dc.description.abstract | 在冷卻水網路設計的文獻中,大部分只討論具有單一個冷卻器網路(heat exchanger network)的冷卻水系統(cooling water system);而本論文則是對於跨廠區的冷卻水網路,意即具有多個冷卻器網路的冷卻水系統,提出一套完整的數學模式,同時此模式也能夠包含過去學者對單一冷卻器網路提出的模式。
本研究對於跨廠區的冷卻水網路,依據工廠需求的操作情況不同,將系統分成五種情境(Scenario A~Scenario E)來討論。首先以目標函數(1)最少冷卻水消耗量,對一個虛擬的例子做五種情境的最適化並比較結果;接著,基於目標函數(1)的結果,更進一步考量系統中其他成本,再以目標函數(2)最小年總成本對五種情境做最適化分析,並比較跨廠區冷卻水整合與只有工廠內部整合成本(或冷卻水)的節省。此外,在不同管線成本下,評估系統作跨廠區整合的潛力。最後,也考慮可選擇的管徑種類有限的情況下計算管線成本,做年總成本最適化。 | zh_TW |
| dc.description.abstract | To date, research in cooling water system has only focused on a single cooling water network. For the purpose to enhance reuse possibilities of cooling water and to further reduce cooling water requirement, the idea of inter-plant cooling water integration was recently proposed. This work aims to develop a mixed-integer nonlinear program (MINLP) formulation for the synthesis of inter-plant cooling water networks based on superstructures. The newly proposed model can be also used to include some other cooling water integration schemes that have been published in literature.
In this work, five different integration schemes are analyzed. For each scheme, two objective functions are considered which involve the minimization of cooling water supply and total annualized cost. In the latter case, two kinds of cost functions are adopted for the estimation of piping cost. An example is used to illustrate the proposed formulation and the optimal results for different schemes are compared with each other. Furthermore, the impact of piping cost on inter-plant cooling water network design is also examined. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-15T01:27:25Z (GMT). No. of bitstreams: 1 ntu-98-R96524079-1.pdf: 12121680 bytes, checksum: 6ce853fb9db4941d1888a7bdde52a7f4 (MD5) Previous issue date: 2009 | en |
| dc.description.tableofcontents | 誌謝 i
摘要 iii Abstract v 附圖目錄 xi 附表目錄 xiii 1緒論 1 1.1前言 1 1.2整合性冷卻水網路設計之發展與型態說明 3 1.3文獻回顧 5 1.4研究動機與目的 7 1.5組織章節 8 2.冷卻水網路之最適化模式建立 9 2.1模式建立之背景說明 9 2.2模式建立之基本假設條件 15 2.3模式建立之圖解說明16 2.4模式之符號、集合、系統參數與系統變數(Indies, Sets, Parameters, Variables) 19 2.4.1下標符號說明(Indies) 19 2.4.2集合說明(Sets) 20 2.4.3系統參數(Parameters) 21 2.4.4系統變數(Variables) 21 2.5冷卻水網路限制式 25 2.5.1冷卻塔流量平衡與能量平衡 25 2.5.2供應儲存槽流量平衡與能量平衡 26 2.5.3冷卻器流量平衡與能量平衡 27 2.5.4中間儲存槽流量平衡與能量平衡 29 2.5.5回流儲存槽流量平衡與能量平衡 30 2.5.6排放儲存槽流量平衡與能量平衡 30 2.5.7管線合併限制式 33 2.5.8物流流量之上下與下限 33 2.5.9跨廠區管限數目限制式 34 2.6五種情境下的額外限制式 35 2.6.1Scenario A 境之額外限制式 35 2.6.2Scenario B 境之額外限制式 35 2.6.3Scenario C 境之額外限制式 36 2.6.4Scenario D 境之額外限制式 37 2.6.5Scenario E 境之額外限制式 37 2.7成本函數 38 2.8目標函數46 2.8.1目標函數(1):最少冷卻水消耗量 46 2.8.1目標函數(2):最小年總成本47 3冷卻水網路最適化之情境模擬與分析結果 49 3.1最適化軟體 50 3.2三個工廠及十五個冷卻器之冷卻水網路情境模擬 50 3.3目標函數(1)最少冷卻水消耗量之模擬結果分析與討論 51 3.4目標函數(2)最小年總成本之模擬結果分析與討論 60 3.4.1目標函數(2)情況下以第一種模式計算管線成本下 改變管線成本的影響分析 67 3.4.2目標函數(2)情況下以第二種模式計算管線成本的 結果分析 70 4.結論與未來展望 75 4.1結論 75 4.2未來展望 76 參考文獻 79 作者簡歷 83 | |
| dc.language.iso | zh-TW | |
| dc.subject | 冷卻水網路 | zh_TW |
| dc.subject | 混合整數非線性規劃 | zh_TW |
| dc.subject | 最適化 | zh_TW |
| dc.subject | Optimization | en |
| dc.subject | Cooling Water Network | en |
| dc.subject | Mixed-interger Nonlinear Program(MINLP) | en |
| dc.title | 應用數學規劃法作跨廠區冷卻水網路之最適化設計 | zh_TW |
| dc.title | Mathematical Programming Approach for the Design of Inter-plant Cooling Water Network | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 97-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 黃孝平,王子奇 | |
| dc.subject.keyword | 最適化,冷卻水網路,混合整數非線性規劃, | zh_TW |
| dc.subject.keyword | Optimization,Cooling Water Network,Mixed-interger Nonlinear Program(MINLP), | en |
| dc.relation.page | 83 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2009-07-23 | |
| 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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