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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/123456789/10012
完整後設資料紀錄
DC 欄位值語言
dc.contributor.advisor吳哲夫
dc.contributor.authorYu-Ti Tsengen
dc.contributor.author曾郁迪zh_TW
dc.date.accessioned2021-05-20T20:55:42Z-
dc.date.available2014-08-04
dc.date.available2021-05-20T20:55:42Z-
dc.date.copyright2011-08-04
dc.date.issued2011
dc.date.submitted2011-07-29
dc.identifier.citation1. Jagadesh D, Kubota N, Yokota M, Sato A, Tavare NS. Large and mono-sized product crystals from natural cooling mode batch crystallizer. Journal of Chemical Engineering of Japan 1996;29(5): 865-73.
2. Jagadesh D, Chivate MR, Tavare NS. Batch Crystallization of Potassium-Chloride by an Ammoniation Process. Industrial & Engineering Chemistry Research 1992;31(2): 561-68.
3. Kubota N, Doki N, Yokota M, Sato A. Seeding policy in batch cooling crystallization. Powder Technology 2001;121(1): 31-38.
4. Doki N, Kubota N, Sato A, Yokota M, Hamada O, Masumi F. Scaleup experiments on seeded batch cooling crystallization of potassium alum. Aiche Journal 1999;45(12): 2527-33.
5. Doki N, Kubota N, Sato A, Yokota M. Effect of cooling mode on product crystal size in seeded batch crystallization of potassium alum. Chemical Engineering Journal 2001;81(1-3): 313-16.
6. Doki N, Kubota N, Yokota M, Chianese A. Determination of critical seed loading ratio for the production of crystals of uni-modal size distribution in batch cooling crystallization of potassium alum. Journal of Chemical Engineering of Japan 2002;35(7): 670-76.
7. Doki N, Kubota N, Yokota M, Kimura S, Sasaki S. Production of sodium chloride crystals of uni-modal size distribution by batch dilution crystallization. Journal of Chemical Engineering of Japan 2002;35(11): 1099-104.
8. Doki N, Yokota M, Nakamura H, Sasaki S, Kubota N. Seeded batch cooling crystallization of adipic acid from ethanol solution. Journal of Chemical Engineering of Japan 2003;36(8): 1001-04.
9. Doki N, Yokota M, Sasaki S, Kubota N. Size distribution of needle-shape crystals of monosodium L-glutamate obtained by seeded batch cooling crystallization. Journal of Chemical Engineering of Japan 2004;37(3): 436-42.
10. Kubota N, Doki N, Yokota M, Sato A. Seeding policy in batch cooling crystallization. Powder Technology 2001;121(1): 31-38.
11. Lung-Somarriba BLM, Moscosa-Santillan M, Porte C, Delacroix A. Effect of seeded surface area on crystal size distribution in glycine batch cooling crystallization: a seeding methodology. Journal of Crystal Growth 2004;270(3-4): 624-32.
12. Hojjati H, Rohani S. Cooling and seeding effect on supersaturation and final crystal size distribution (CSD) of ammonium sulphate in a batch crystallizer. Chemical Engineering and Processing 2005;44(9): 949-57.
13. Chung SH, Ma DL, Braatz RD. Optimal seeding in batch crystallization. Canadian Journal of Chemical Engineering 1999;77(3): 590-96.
14. Mullin JW, Nyvlt J. Programmed Cooling of Batch Crystallizers. Chemical Engineering Science 1971;26(3): 369-377.
15. Ward JD, Yu CC, Doherty MF. A New Framework and a Simpler Method for the Development of Batch Crystallization Recipes. Aiche Journal 2011;57(3): 606-17.
16. Hulburt HM, Katz S. Some Problems in Particle Technology - a Statistical Mechanical Formulation. Chemical Engineering Science 1964;19(8): 555-74.
17. Mersmann, A. Ed. Crystallization Technology Handbook. New York: Marcel Dekker, 2001.
18. Nyvlt, J. Design of Crystallizers. Boca Raton, FL: CRC Press, 1992.
19. Ramkrishna D. Population Balances. San Diego: Academic Press,2000.
20. Randolph, AD. Larson MA. Theory of Particulate Processes. New York: Academic Press, 1988.
21. Tavare, NS. Industrial Crystallization: Process Simulation Analysis and Design. New York: Plenum Press, 1995.
22. Rohani S, Sarkar D, Jutan A. Multi-objective optimization of semibatch reactive crystallization processes. Aiche Journal 2007;53(5): 1164-77.
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/10012-
dc.description.abstract在此研究中我們對於批次結晶程序做了整體性的分析及探討。首先我們探討了給予長晶速率限制條件對程序的影響。對於特定操作條件我們發現增加限制條件對於產品品質沒有顯著影響。接著我們探討晶種負載率的影響。我們發現提高晶種負載率能更有效率壓制成核以及成核速率。另外此研究中我們透過電腦模擬針對兩個結晶系統以及無因次系統做了晶種分析圖。對於臨界晶種負載率我們導出無因次的關係式,研究發現此關係式對於預測模擬結果有很高的準確度。我們探討了臨界晶種總表面積以及臨界晶種總長度,然而這兩個變數不建議做為設計變數。此研究中我們也探討了總反應時間以及淨結晶產量對於批次結晶程序的影響,結果可用做設計結晶程序的簡單方針。zh_TW
dc.description.abstractIn this work we investigate the development of recipes for seeded batch crystallization processes. First we investigate the effect of growth rate constraint. For a particular case we find that such a constraint does not have a significant influence on product quality. Then we investigate the effect of seed loading. We find that the seed mass has a large influence on decreasing the final nuclei mass and efficiently suppressed the nucleation rate. In this work seed charts for two dimensional systems and the dimensionless system are produced and used to determine critical seed loading ratio by computer simulation. An analytical expression for the critical seed loading is derived and simulation results show high accuracy for predicting critical seed loading ratio versus dimensionless seed mean size using constant growth rate trajectory. We investigate two critical values which are critical seed surface area and critical seed total length. However these two critical values are not recommended to use as the design variables. In this work we also investigate the effect of total batch time and the net crystal yield on the batch process, and the results can be used as the design guideline.en
dc.description.provenanceMade available in DSpace on 2021-05-20T20:55:42Z (GMT). No. of bitstreams: 1
ntu-100-R98524061-1.pdf: 1243578 bytes, checksum: 97759f4a5994e536076c50e3c0276258 (MD5)
Previous issue date: 2011
en
dc.description.tableofcontents誌謝 i
摘要 ii
Abstract iii
Table of Content iv
List of Figures vi
List of Tables ix
1 Introduction 1
1.1 Overview 1
1.2 Seeding policy 3
1.3 Literature survey 5
1.4 Thesis Organization 7
2 Modeling of crystallization systems 8
3 Case study systems 18
3.1 Case Study 18
3.2 Growth rate constraint 23
4 Analytical expressions of critical seed loading ratio 28
4.1 Overview 28
4.2 Simulation result 33
5 Seed Charts 38
5.1 Overview 38
5.2 Seed chart and empirical Equation 39
5.3 Critical seed loading ratio with different kinetic parameters 53
6 Notion of critical seed surface area 55
7 Relationship between batch time, seed loading, and net crystal yield 65
7.1 Effect of batch time tf 65
7.2 Effect of net crystal yield 75
7.3 Design guideline 76
8 Conclusions 77
9 References 79
dc.language.isoen
dc.title批次結晶程序整體設計之發展zh_TW
dc.titleDevelopment of recipes for seeded batch crystallizationen
dc.typeThesis
dc.date.schoolyear99-2
dc.description.degree碩士
dc.contributor.oralexamcommittee錢義隆,陳誠亮,蕭立鼎
dc.subject.keyword長晶速率限制,臨界晶種負載率,總反應時間,淨結晶產量,zh_TW
dc.subject.keywordgrowth rate constraint,critical seed loading ratio,total batch time,the net crystal yield,en
dc.relation.page82
dc.rights.note同意授權(全球公開)
dc.date.accepted2011-07-29
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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