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| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 黃孝平(Hsiao-Ping Huang) | |
| dc.contributor.author | Yuan-Chieh Ho | en |
| dc.contributor.author | 何元傑 | zh_TW |
| dc.date.accessioned | 2021-06-15T01:30:49Z | - |
| dc.date.available | 2009-07-29 | |
| dc.date.copyright | 2009-07-29 | |
| dc.date.issued | 2009 | |
| dc.date.submitted | 2009-07-21 | |
| dc.identifier.citation | [1] Wright, R.O.; N.J.Elizabeth, Fractionation Apparatus. US Patent 1949
[2] Triantafyllou, C.; Smith, R., The Design and Optimization of Fully Thermally Coupled Distillation-Columns. Trans. Inst. Chem. Eng. 1992, 70, (2), 118-132. [3] Lestak, F.; Smith, R.; Dhole, V. R., Heat-Transfer across the Wall of Dividing Wall Columns. Trans. Inst. Chem. Eng. 1994, 72, (A5), 639-644. [4] Mutalib, M. I. A.; Smith, R., Operation and control of dividing wall distillation columns - Part 1: Degrees of freedom and dynamic simulation. Trans. Inst. Chem. Eng. 1998, 76, (A3), 308-318. [5] Mutalib, M. I. A.; Zeglam, A. O.; Smith, R., Operation and control of dividing wall distillation columns - Part 2: Simulation and pilot plant studies using temperature control. Trans. Inst. Chem. Eng. 1998, 76, (A3), 319-334. [6] Amminudin, K. A.; Smith, R.; Thong, D. Y. C.; Towler, G. P., Design and optimization of fully thermally coupled distillation columns part 1: Preliminary design and optimization methodology. Trans. Inst. Chem. Eng. 2001, 79, (A7), 701-715. [7] Amminudin, K. A.; Smith, R., Design and optimization of fully thermally coupled distillation columns part 2: Application of dividing wall columns in retrofit. Trans. Inst. Chem. Eng. 2001, 79, (A7), 716-724. [8] Wolff, E. A.; Skogestad, S., Operation of Integrated 3-Product (Petlyuk) Distillation-Columns. Ind. Eng. Chem. Res. 1995, 34, (6), 2094-2103. [9] Christiansen, A. C.; Skogestad, S.; Lien, K., Partitioned Petlyuk arrangements for quaternary separations. Distillation and Absorption '97, Vols 1 and 2 1997, (142), 745-756 1040. [10] Christiansen, A. C.; Skogestad, S.; Lien, K., Complex distillation arrangements: Extending the Petlyuk ideas. Comput. Chem. Eng 1997, 21, S237-S242. [11] Halvorsen, I. J.; Skogestad, S., Optimizing control of Petlyuk distillation: Understanding the steady-state behavior. Comput. Chem. Eng 1997, 21, S249-S254. [12] Halvorsen, I. J.; Skogestad, S., Optimal operation of Petlyuk distillation: steady-state behavior. J. Process Control 1999, 9, (5), 407-424. [13] Halvorsen, I. J.; Skogestad, S., Minimum energy consumption in multicomponent distillation. 1. V-min diagram for a two-product column. Ind. Eng. Chem. Res. 2003, 42, (3), 596-604. [14] Halvorsen, I. J.; Skogestad, S., Minimum energy consumption in multicomponent distillation. 2. Three-product Petlyuk arrangements. Ind. Eng. Chem. Res. 2003, 42, (3), 605-615. [15] Halvorsen, I. J.; Skogestad, S., Minimum energy consumption in multicomponent distillation. 3. More than three products and generalized Petlyuk arrangements. Ind. Eng. Chem. Res. 2003, 42, (3), 616-629. [16] Halvorsen, I. J.; Skogestad, S., Shortcut analysis of optimal operation of petlyuk distillation. Ind. Eng. Chem. Res. 2004, 43, (14), 3994-3999. [17] Kim, Y. H., Structural design and operation of a fully thermally coupled distillation column. Chem. Eng. J. 2002, 85, (2-3), 289-301. [18] Kim, Y. H.; Nakaiwa, M.; Hwang, K. S., Approximate design of fully thermally coupled distillation columns. Korean J. Chem. Eng. 2002, 19, (3), 383-390. [19] Agrawal, R.; Fidkowski, Z. T., Are thermally coupled distillation columns always thermodynamically more efficient for ternary distillations? Ind. Eng. Chem. Res. 1998, 37, (8), 3444-3454. [20] Agrawal, R.; Fidkowski, Z. T., More operable arrangements of fully thermally coupled distillation columns. AIChE J. 1998, 44, (11), 2565-2568. [21] Underwood, A. J. V., Fractional Distillation of Multicomponent Mixtures. Chem. Eng. Prog. 1948, 44, (8), 603-614. [22] Fidkowski, Z.; Krolikowski, L., Thermally Coupled System of Distillation-Columns - Optimization Procedure. AIChE J. 1986, 32, (4), 537-546. [23] Glinos, K. N.; Malone, M. F., Design of Sidestream Distillation-Columns. Ind. Eng. Chem. Process Des. Dev. 1985, 24, (3), 822-828. | |
| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/42967 | - |
| dc.description.abstract | 本論文提出了一個新的觀點，藉由此觀點分析三種不同型式的內隔壁式蒸餾塔，可以直覺地了解，為何內隔壁式蒸餾塔相較於其對應的傳統蒸餾塔架構時，會比較省能。而透過此觀點逐步分析內隔壁式蒸餾塔後，更可以發現內隔壁式蒸餾塔的能耗，與傳統蒸餾塔架構中再混和(remixing)現象之間的關係，進而推導出一系列的解析公式，可針對再混和的程度，估計出內隔壁式蒸餾塔的省能潛能。論文的最後，舉了文獻上常見的三種真實系統作為例子，檢驗這些解析公式的估計結果，並加以討論。 | zh_TW |
| dc.description.abstract | A new framework is introduced to analyze divided wall columns. The framework provides a simple and intuitive understanding of why three different types of divided wall columns save energy when they are compared with corresponding conventional columns. Furthermore, analytical expressions are derived to quantify the potential energy saving of divided wall columns based on remixing. The method is illustrated with some real mixture examples often seen in literature. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-15T01:30:49Z (GMT). No. of bitstreams: 1 ntu-98-R96524059-1.pdf: 1008077 bytes, checksum: e823c6141e9b8b11899b0347d485bb0f (MD5) Previous issue date: 2009 | en |
| dc.description.tableofcontents | 致謝 I
摘要 III Abstract V 目錄 VI 圖目錄 VIII 表目錄 X 1 緒論 1 1.1 前言 1 1.2 文獻回顧 2 1.3 研究動機與目的 3 1.4 組織章節 4 2內隔壁式蒸餾塔的最小能耗 5 2.1 三種不同類型的內隔壁式蒸餾塔 5 2.1.1 DWCL 5 2.1.2 DWCU 6 2.1.3 DWCM 8 2.2 使用Underwood’s method計算最小能耗 9 2.2.1 DWCL 10 2.2.2 DWCU 12 2.2.3 DWCM 15 2.3 Underwood’s method計算過程之觀察 18 3 解析式的推導 19 3.1 內隔壁式蒸餾塔的節能解釋 19 3.1.1 DWCL 19 3.1.2 DWCU 22 3.1.3 DWCM 25 3.2 公式推導 27 3.2.1 DWCL 28 3.2.2 DWCU 37 3.2.3 DWCM 46 3.3 針對解析式的觀察結果 50 3.4 解析式的限制及延伸 50 4 真實系統 53 4.1 分析方法與步驟 53 4.2 文獻上的例子 55 4.2.1 Benzene, Toluene, Ethyl Benzene 55 4.2.2 n-Butane, Isopentane, n-Pentane 62 4.2.3 n-Pentane, n-Hexane, n-Heptane 69 4.3 結果討論 76 5 結論 82 符號說明 83 參考文獻 85 附錄A 88 附錄B 89 附錄C 90 | |
| dc.language.iso | zh-TW | |
| dc.title | 依據再混合的程度定量估計內隔壁式蒸餾塔的節能效果 | zh_TW |
| dc.title | Quantify Potential Energy Saving of Divided Wall Column Based on Degree of Remixing | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 97-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 陳誠亮(Cheng-Liang Chen),Jeffrey D. Ward(Jeffrey D. Ward),汪上曉(DAVID SHAN-HILL WONG),王聖潔 | |
| dc.subject.keyword | 再混合,內隔壁式蒸餾塔,能源, | zh_TW |
| dc.subject.keyword | Divided Wall Column,Remixing,energy, | en |
| dc.relation.page | 91 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2009-07-21 | |
| 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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