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| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 吳哲夫(Jeffrey D. Ward) | |
| dc.contributor.author | Teng-Yun Mao | en |
| dc.contributor.author | 茆騰允 | zh_TW |
| dc.date.accessioned | 2021-06-16T23:39:58Z | - |
| dc.date.available | 2012-08-03 | |
| dc.date.copyright | 2012-08-03 | |
| dc.date.issued | 2012 | |
| dc.date.submitted | 2012-07-25 | |
| dc.identifier.citation | 1. Wright, R.O.; Elizabeth, N.J., Fractional apparatus. US Patent, 1949. 2,471,134.
2. Triantafyllou, C.; Smith, R, The Design and Optimization of fully thermally coupled distillation-columns. Chem. Eng. Res. Des., 1992. 70: p. 118-132. 3. 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. Chem. Eng. Res. Des., 2001. 79: p. 701-715. 4. Kim, Y.H., Structural design and operation of a fully thermally coupled distillation column. Chem. Eng. J., 2002. 85: p. 289-301. 5. Lek, C.M.; Rangaiah, G.P.; Hidajat, K., Distillation: Revisiting some rules of thumb. Chen. Eng., 2004. 111: p. 50-55. 6. Muralikrishna, K.; Madhavan, K.P.; Shah, S.S., Development of dividing wall distillation column design space for a specified separation. Chem. Eng. Res. Des., 2002. 80: p. 155-166. 7. Sotudeh, N.; Shahraki, B. H., A Method for the Design of Divided Wall Columns. Chemical Engineering & Technology, 2007. 30(9): p. 1284-1291. 8. Ram’ırez-Corona, N.; Jim’enez-Guti’errez, A.; Castro-Ag‥uero, A.; Rico-Ram’ırez, V., Optimum Design of Petluk and Divided-wall distillation systems using a shortcut model. Chem. Eng. Res. Des., 2008. 9. Chu, K.T.; Cadoret, L.; Yu, C.C.; Ward, J. D., A New Shortcut Design Method and Economic Analysis of Divided Wall Columns. Industrial & Engineering Chemistry Research, 2011. 50(15): p. 9221-9235. 10. Agrawal, R.; Fidkowski, Z.T., Are thermally coupled distillation columns always thermodynamically more efficient for ternary distillations? Ind. Eng. Chem. Res., 1998. 37: p. 3444-3454. 11. Rev, E.; Emtir, M.; Szitkai, Z.; Mizsey, P.; Fonyo, Z., Energy savings of integrated and coupled distillation systems. Comput. Chem. Eng., 2001. 25: p. 119-140. 12. Errico, M.; Tola, G.; Rong, B.G. Demurtas, D.; Turunen,I., Energy saving and capital cost evaluation in distillation column sequences with a divided wall column. Chem. Eng. Res. Des., 2009. 87: p. 1649-1657. 13. Wolff, E.A.; Skogestad, S., Operation of integrated 3-product (Petlyuk) distillation-columns. Ind. Eng. Chem. Res., 1995. 34: p. 2094-2103. 14. Mutalib, M.I.A.; Smith, R., Operation and control of dividing wall distillation columns - Part 1: Degrees of freedom and dynamic simulation. Chem. Eng. Res. Des., 1998. 76: p. 308-318. 15. 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. Chem. Eng. Res. Des., 1998. 76: p. 319-334. 16. Halvorsen, I.J.; Skogestad, S., Optimal operation of Petlyuk distillation: steady-state behavior. Journal of Process Control, 1999. 9: p. 407-424. 17. Serra, M.; Perrier, M.; Espuna, A.; Puigjaner, L., Analysis of different control possibilities for the divided wall column: feedback diagonal and dynamic matrix control. Comput. Chem. Eng., 2001. 25: p. 859-866. 18. Serra, M.; Perrier, M.; Espuna, A.; Puigjaner, L., Controllability of different multicomponent distillation arrangements. Ind. Eng. Chem. Res., 2003. 42: p. 1773-1782. 19. Adrian, T.; Schoenmakers, H.; Boll, M. Model predictive control of integrated unit operations: Control of a divided wall column. Chem. Eng. Process., 2003. 43: p. 347-355. 20. Wang, S.J.; Wang, D.S.H., Controllability and energy efficiency of a high-purity divided wall column. Chem. Eng. Sci, 2007. 62: p. 1010-1025. 21. Cho, Y.; Kim, B.; Kim, D. Han, M.; Lee, M., Operation of divided wall column with vapor sidedraw using profile position control. Journal of Process Control, 2009. 19: p. 932-941. 22. Ling, H.; Luyben, W.L., New control structure for divided-wall columns. Ind. Eng. Chem. Res., 2009. 48: p. 6034-6049. 23. 黃琦聰; 黃聖夫; 方淞, 分隔內壁蒸餾塔簡介. 化工技術, 2006. 14(7): p. 105-113. 24. Holland, S.T.; Abbas, R.; Hildebrandt, D.; Glasser, D., Complex column design by application of column profile map techniques: sharp-split Petlyuk column design. Ind. Eng. Chem. Res., 2010. 49: p. 327-349. 25. Douglas, J.M., Conceptual Design of Chemical Processes. 1988 | |
| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/65386 | - |
| dc.description.abstract | 相較於傳統的蒸餾序列，內隔壁式蒸餾塔（DWC）可以節省更多的能量與與設備成本。然而，內隔壁式蒸餾塔在設計上也較為困難，因為較傳統序列擁有更多的設計自由度。在本研究中，我們針對三種型態之分隔式蒸餾塔設計出一套捷徑式設計法以應用於非理想系統中。以文獻回顧中提到的設計方法為基礎，加以修正改良。最主要的改變是採用Aspen Plus為模擬工具，此舉可以使設計方法不必在基於失真的固定相對揮發度假說，能夠應用在相對揮發度隨著溫度改變較大的系統中。研究中包含一系列的嚴謹模擬和兩個實例探討以測試此設計方法之實用性。結果顯示設計方法計算出的年度成本和最小年度成本相去無幾，而我們也可以應用此方法來做為嚴謹設計時的一項指標。 | zh_TW |
| dc.description.abstract | Divided-wall columns (DWCs) can save energy and capital cost compared with traditional distillation columns. However the design of DWCs is more difficult because there are more degrees of freedom. In this work, we develop a general design method for non-ideal systems for all three types of DWCs. Based on the design method by literature, we make some evolutions. The main modification is to use Aspen Plus simulation instead of the short cut equation based on constant relative volatility assumption. A series of rigorous simulations are applied to two real systems in order to show the performance. The results show that the total annual cost (TAC) based on the design method is close to the minimum total annual cost. Finally the manipulate variable designed can be used as the initial guess of the optimal total annual cost design case. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-16T23:39:58Z (GMT). No. of bitstreams: 1 ntu-101-R99524064-1.pdf: 1661307 bytes, checksum: 38497ec1be5a2fd8ab254dc47b3a280d (MD5) Previous issue date: 2012 | en |
| dc.description.tableofcontents | 致謝 i
Abstract ii 摘要 iii 1 Content iv 2 List of Figures viii 3 List of Tables xxii 1 Introduction 1 1.1 Overview 1 1.2 Introduction for three types of DWCs 3 1.2.1 DWCL 4 1.2.2 DWCU 5 1.2.3 DWCM 6 1.3 Literature survey 8 1.4 Motivation 14 1.5 Dissertation organization 14 2 Model and shortcut design validation 16 2.1 Overview 16 2.2 Shortcut design method for DWCs 17 2.2.1 DWCL 17 2.2.2 DWCU 26 2.2.3 DWCM 35 2.3 Design method of DWCs in real system 51 2.3.1 Validations in real system 51 2.3.2 Minimum conditions simulation of DWCL 52 2.3.3 Minimum conditions simulation of DWCU 55 2.3.4 Minimum conditions simulation of DWCM 58 2.4 Analysis method 60 2.4.1 Purity difference 61 2.4.2 Total annual cost (TAC) and optimization 62 2.4.3 Column details 66 3 Real case studies 66 3.1 Case study 1 66 3.1.1 DWCL 68 3.1.2 DWCU 78 3.1.3 DWCM 87 3.2 Case study 2 96 3.2.1 DWCL 97 3.2.2 DWCU 107 3.2.3 DWCM 116 3.3 Result comparison 125 3.3.1 Comparison with geometric mean method 126 3.3.2 Comparison with Chu’s[9] work 133 4 Conclusion 137 Appendix A[25] 138 5 References 140 | |
| dc.language.iso | zh-TW | |
| dc.subject | 熱整合塔 | zh_TW |
| dc.subject | 捷徑式設計 | zh_TW |
| dc.subject | 內隔壁式蒸餾塔 | zh_TW |
| dc.subject | 非理想系統 | zh_TW |
| dc.subject | thermal coupling column | en |
| dc.subject | divided wall column | en |
| dc.subject | shortcut design | en |
| dc.subject | non-ideal systems | en |
| dc.title | 內隔壁式蒸餾塔應用於非理想系統之穩態設計 | zh_TW |
| dc.title | Steady State Design of Non-ideal Divided Wall Column systems | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 100-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 陳誠亮(Cheng-Liang Chen),錢義隆(I-Lung Chien),汪上曉,鄭西顯 | |
| dc.subject.keyword | 熱整合塔,內隔壁式蒸餾塔,捷徑式設計,非理想系統, | zh_TW |
| dc.subject.keyword | thermal coupling column,divided wall column,shortcut design,non-ideal systems, | en |
| dc.relation.page | 141 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2012-07-25 | |
| 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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