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Journal articles on the topic 'Multicomponent Batch Distillation System'

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Published: 4 June 2021
Last updated: 13 February 2022

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1

Luyben, William L. "Multicomponent batch distillation. 1. Ternary systems with slop recycle." Industrial & Engineering Chemistry Research 27, no. 4 (April 1988): 642–47. http://dx.doi.org/10.1021/ie00076a019.

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2

Barolo, M., and G. B. Guarise. "Batch Distillation of Multicomponent Systems with Constant Relative Volatilities." Chemical Engineering Research and Design 74, no. 8 (November 1996): 863–71. http://dx.doi.org/10.1205/026387696523166.

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3

Reuter, E., G. Wozny, and L. Jeromin. "Modeling of multicomponent batch distillation processes with chemical reaction and their control systems." Computers & Chemical Engineering 13, no. 4-5 (April 1989): 499–510. http://dx.doi.org/10.1016/0098-1354(89)85032-x.

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4

Al-Tuwaim, Mohammad S., and William L. Luyben. "Multicomponent batch distillation. 3. Shortcut design of batch distillation columns." Industrial & Engineering Chemistry Research 30, no. 3 (March 1991): 507–16. http://dx.doi.org/10.1021/ie00051a011.

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5

Diwekar, Urmila M., and K. P. Madhavan. "Multicomponent batch distillation column design." Industrial & Engineering Chemistry Research 30, no. 4 (April 1991): 713–21. http://dx.doi.org/10.1021/ie00052a014.

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6

Ahmad, Berit S., and Paul I. Barton. "Homogeneous multicomponent azeotropic batch distillation." AIChE Journal 42, no. 12 (December 1996): 3419–33. http://dx.doi.org/10.1002/aic.690421212.

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7

Diwekar, Urmilla, K. P. Madhavan, and R. E. Swaney. "Optimization of multicomponent batch distillation columns." Industrial & Engineering Chemistry Research 28, no. 7 (July 1989): 1011–17. http://dx.doi.org/10.1021/ie00091a019.

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8

CHIOTTI, OMAR J., HECTOR E. SALOMONE, and OSCAR A. IRIBARREN. "SELECTION OF MULTICOMPONENT BATCH DISTILLATION SEQUENCES." Chemical Engineering Communications 119, no. 1 (January 1993): 1–21. http://dx.doi.org/10.1080/00986449308936104.

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9

Galindez, H., and Aa Fredenslund. "Simulation of multicomponent batch distillation processes." Computers & Chemical Engineering 12, no. 4 (April 1988): 281–88. http://dx.doi.org/10.1016/0098-1354(88)85039-7.

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10

Kim, Jeung Kun, and Dong Pyo Ju. "Multicomponent batch distillation with distillate receiver." Korean Journal of Chemical Engineering 20, no. 3 (May 2003): 522–27. http://dx.doi.org/10.1007/bf02705559.

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11

Carlos Gómez, Juan, and Marta Basualdo. "Nonlinear Identification of Multicomponent Batch Distillation Processes." IFAC Proceedings Volumes 33, no. 10 (June 2000): 953–58. http://dx.doi.org/10.1016/s1474-6670(17)38663-9.

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12

Venkateswarlu, C., and S. Avantika. "Optimal state estimation of multicomponent batch distillation." Chemical Engineering Science 56, no. 20 (October 2001): 5771–86. http://dx.doi.org/10.1016/s0009-2509(01)00284-6.

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13

Sharif, M., N. Shah, and C. C. Pantelides. "On the design of multicomponent batch distillation columns." Computers & Chemical Engineering 22 (March 1998): S69—S76. http://dx.doi.org/10.1016/s0098-1354(98)00040-4.

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14

Mujtaba, I. M., and S. Macchietto. "An optimal recycle policy for multicomponent batch distillation." Computers & Chemical Engineering 16 (May 1992): S273—S280. http://dx.doi.org/10.1016/s0098-1354(09)80032-x.

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15

Yildiz, U., U. A. Gurkan, C. Özgen, and K. Leblebicioğlu. "State Estimator Design for Multicomponent Batch Distillation Columns." Chemical Engineering Research and Design 83, no. 5 (May 2005): 433–44. http://dx.doi.org/10.1205/cherd.03318.

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16

Binous, Housam, Mamdouh A. Al-Harthi, and Ahmed Bellagi. "Experimental and theoretical study of multicomponent batch distillation." Computer Applications in Engineering Education 23, no. 6 (April 15, 2015): 813–23. http://dx.doi.org/10.1002/cae.21652.

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17

Kreul, L. U., A. Górak, and P. I. Barton. "Dynamic rate-based model for multicomponent batch distillation." AIChE Journal 45, no. 9 (September 1999): 1953–62. http://dx.doi.org/10.1002/aic.690450912.

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18

Bonny, L., S. Domenech, P. Floquet, and L. Pibouleau. "Recycling of slop cuts in multicomponent batch distillation." Computers & Chemical Engineering 18 (January 1994): S75—S79. http://dx.doi.org/10.1016/0098-1354(94)80013-8.

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19

Bernot, Christine, Michael F. Doherty, and Michael F. Malone. "Feasibility and separation sequencing in multicomponent batch distillation." Chemical Engineering Science 46, no. 5-6 (1991): 1311–26. http://dx.doi.org/10.1016/0009-2509(91)85058-6.

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20

Quintero-Marmol, Enrique, and William L. Luyben. "Inferential model-based control of multicomponent batch distillation." Chemical Engineering Science 47, no. 4 (1992): 887–98. http://dx.doi.org/10.1016/0009-2509(92)80274-g.

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21

Bernon, Christine, Michael F. Doherty, and Michael F. Malone. "Patterns of composition change in multicomponent batch distillation." Chemical Engineering Science 45, no. 5 (1990): 1207–21. http://dx.doi.org/10.1016/0009-2509(90)87114-8.

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22

Basualdo, Marta S., Carlos A. Ruiz, and Nicolás J. Scenna. "Simulation of Multicomponent Batch Distillation with Chemical Reactions Processes." IFAC Proceedings Volumes 28, no. 9 (June 1995): 191–96. http://dx.doi.org/10.1016/s1474-6670(17)47038-8.

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23

Bernot, Christine, Michael F. Doherty, and Michael F. Malone. "Design and operating targets for nonideal multicomponent batch distillation." Industrial & Engineering Chemistry Research 32, no. 2 (February 1993): 293–301. http://dx.doi.org/10.1021/ie00014a008.

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24

Hitch, David M., and Ronald W. Rousseau. "Simulation of continuous-contact separation processes: multicomponent batch distillation." Industrial & Engineering Chemistry Research 27, no. 8 (August 1988): 1466–73. http://dx.doi.org/10.1021/ie00080a019.

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25

Diwekar, Urmila, and Claudio Rivier. "Missing Components in Multicomponent Batch Distillation and Optimal Control." Industrial & Engineering Chemistry Research 58, no. 37 (August 28, 2019): 17455–61. http://dx.doi.org/10.1021/acs.iecr.9b02242.

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26

Mori, Hideki, Hiroki Goto, Zhi Cai Yang, Tsutomu Aragaki, Seung-Tae Koh, and Iwao Akiba. "A Stagewise Algorithm for Multicomponent Multistage Batch Distillation Calculation." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 28, no. 5 (1995): 576–81. http://dx.doi.org/10.1252/jcej.28.576.

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27

Barolo, Massimiliano, and Fabrizio Berto. "Composition Control in Batch Distillation: Binary and Multicomponent Mixtures." Industrial & Engineering Chemistry Research 37, no. 12 (December 1998): 4689–98. http://dx.doi.org/10.1021/ie980439o.

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28

Kim, Jeung Kun, and Dong Pyo Ju. "Shortcurt Procedure for Multicomponent Batch Distillation with Distillate Receiver." Industrial & Engineering Chemistry Research 38, no. 3 (March 1999): 1024–31. http://dx.doi.org/10.1021/ie9805584.

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29

Kim, Jeung Kun, and Dong Pyo Ju. "Shortcurt Procedure for Multicomponent Batch Distillation with Distillate Receiver." Industrial & Engineering Chemistry Research 38, no. 3 (March 1999): 1176. http://dx.doi.org/10.1021/ie991081e.

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30

Bonny, L., S. Domenech, P. Floquet, and L. Pibouleau. "Strategies for slop cut recycling in multicomponent batch distillation." Chemical Engineering and Processing: Process Intensification 33, no. 1 (March 1994): 23–31. http://dx.doi.org/10.1016/0255-2701(94)87003-9.

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31

García, A. N., J. C. Z. Loría, A. R. Marín, and A. V. C. Quiroz. "Simple multicomponent batch distillation procedure with a variable reflux policy." Brazilian Journal of Chemical Engineering 31, no. 2 (June 2014): 531–42. http://dx.doi.org/10.1590/0104-6632.20140312s00001590.

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32

Jiménez, L., M. S. Basualdo, J. C. Gómez, L. Toselli, and M. Rosa. "Nonlinear dynamic modeling of multicomponent batch distillation: a case study." Brazilian Journal of Chemical Engineering 19, no. 3 (July 2002): 307–17. http://dx.doi.org/10.1590/s0104-66322002000300006.

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33

Yildiz, Ugur, Evren Güner, Canan Özgen, and Kemal Leblebicioglu. "EKF and ANFIS Estimator Design in Multicomponent Batch Distillation Columns." IFAC Proceedings Volumes 37, no. 9 (July 2004): 631–36. http://dx.doi.org/10.1016/s1474-6670(17)31880-3.

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34

Murlidhar, Gundale Mangesh, and Amiya Kumar Jana. "Nonlinear adaptive control algorithm for a multicomponent batch distillation column." Chemical Engineering Science 62, no. 4 (February 2007): 1111–24. http://dx.doi.org/10.1016/j.ces.2006.11.006.

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35

Diwekar, U. M., R. K. Malik, and K. P. Madhavan. "Optimal reflux rate policy determination for multicomponent batch distillation columns." Computers & Chemical Engineering 11, no. 6 (January 1987): 629–37. http://dx.doi.org/10.1016/0098-1354(87)87008-4.

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36

Mujtaba, I. M., and S. Macchietto. "Optimal operation of multicomponent batch distillation—multiperiod formulation and solution." Computers & Chemical Engineering 17, no. 12 (December 1993): 1191–207. http://dx.doi.org/10.1016/0098-1354(93)80099-9.

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37

Tomazi, Keith G. "Limitations and Dynamics Imposed on Multicomponent Batch Distillation by Tray Hydraulics." Industrial & Engineering Chemistry Research 36, no. 10 (October 1997): 4273–81. http://dx.doi.org/10.1021/ie9702340.

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38

Wajge, R. M., and G. V. Reklaitis. "An Optimal Campaign Structure for Multicomponent Batch Distillation with Reversible Reaction." Industrial & Engineering Chemistry Research 37, no. 5 (May 1998): 1910–16. http://dx.doi.org/10.1021/ie970527t.

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39

Venkateswarlu, Ch, and B. Jeevan Kumar. "Composition estimation of multicomponent reactive batch distillation with optimal sensor configuration." Chemical Engineering Science 61, no. 17 (September 2006): 5560–74. http://dx.doi.org/10.1016/j.ces.2006.04.023.

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40

Adesina, Kehinde Adewale, and C. Abiodun Popoola. "Exergy Rate Profile of Multicomponent Distillation System." International Journal of Recent Contributions from Engineering, Science & IT (iJES) 4, no. 2 (July 5, 2016): 29. http://dx.doi.org/10.3991/ijes.v4i2.5710.

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Abstract:
Exergy rate profiles, exergetic efficiency and irreversibility were used to examine the driving forces in multicomponent distillation system with the view to identifying feasible and efficient operating parameters. The mixture used comprised of 5% propane, 15% iso-butane, 25% nbutane, 20% iso-pentane and 35% n-pentane. Operating variables were feed temperature (-30 oC and -80 oC), pressure (800 kPa and 1200 kPa), and reflux-ratio (2 and 6). Stage-by-stage system exergy analysis was estimated. Column profiles of base case -30 oC, -80 oC, -30 oC-reflus ratio 6, -80 oC reflux ratio 6 and base case reflux ratio 6 did not crossed thus are thermodynamically feasible. Base case -30 oC-reflux ratio 2, -80 oC-reflux ratio 2, and base case-reflux ratio 2 were crossed and constricted and are infeasible. Base case results gave efficiency of 81.7% at depropanizer and 65.2% at debutanizer. Base cases sensitivity results with -30 oC, -80 oC and reflux ratio 6, efficiency range 57.40 – 70% and 65.20% - 54.90% for depropanizer and debutanizer respectively. Spitted cases gave 81.7% and 62.20% with more scatter profiles. Splitted feed base case -30 oC design gave the lowest overall system exergy loss rate of 1.12E+6 and efficiency of 95.70%. Design feasible parameters, system efficiency and irreversibility which form basis
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41

MERT, Suha Orçun. "Performance Assessment of a Batch Distillation System." International Journal of Thermodynamics 18, no. 2 (June 13, 2015): 143. http://dx.doi.org/10.5541/ijot.5000099666.

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42

Pommier, S., S. Massebeuf, B. Kotai, P. Lang, O. Baudouin, P. Floquet, and V. Gerbaud. "Heterogeneous batch distillation processes: Real system optimisation." Chemical Engineering and Processing: Process Intensification 47, no. 3 (March 2008): 408–19. http://dx.doi.org/10.1016/j.cep.2007.01.022.

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43

Ceylan, Hatice, and Canan Özgen. "DYNAMIC MODELLING AND OPTIMAL CONTROL OF A MULTICOMPONENT BATCH PACKED DISTILLATION COLUMN." IFAC Proceedings Volumes 41, no. 2 (2008): 4548–53. http://dx.doi.org/10.3182/20080706-5-kr-1001.00765.

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44

Quintero-Marmol, Enrique, and Wiliam L. Luyben. "Multicomponent batch distillation. 2. Comparison of alternative slop handling and operating strategies." Industrial & Engineering Chemistry Research 29, no. 9 (September 1990): 1915–21. http://dx.doi.org/10.1021/ie00105a025.

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45

Wajge, R. M., J. M. Wilson, J. F. Pekny, and G. V. Reklaitis. "Investigation of Numerical Solution Approaches to Multicomponent Batch Distillation in Packed Beds." Industrial & Engineering Chemistry Research 36, no. 5 (May 1997): 1738–46. http://dx.doi.org/10.1021/ie960296a.

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46

Narvaes-Garcia, A., J. C. Zavala-Loria, L. E. Vilchiz-Bravo, and J. A. Rocha-Uribe. "PERFORMANCE INDICES TO DESIGN A MULTICOMPONENT BATCH DISTILLATION COLUMN USING A SHORTCUT METHOD." Brazilian Journal of Chemical Engineering 32, no. 2 (June 2015): 595–608. http://dx.doi.org/10.1590/0104-6632.20150322s00003157.

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47

Quintero-Marmol, Enrique, William L. Luyben, and Christos Georgakis. "Application of an extended Luenberger observer to the control of multicomponent batch distillation." Industrial & Engineering Chemistry Research 30, no. 8 (August 1991): 1870–80. http://dx.doi.org/10.1021/ie00056a029.

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48

KUROOKA, TAKETOSHI, HIROKAZU NISHITANI, SHINJI HASEBE, and IORI HASHIMOTO. "Energy Conservation by Multi-Effect Batch Distillation System." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 34, no. 9 (2001): 1141–46. http://dx.doi.org/10.1252/jcej.34.1141.

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49

Denes, F., P. Lang, G. Modla, and X. Joulia. "New double column system for heteroazeotropic batch distillation." Computers & Chemical Engineering 33, no. 10 (October 2009): 1631–43. http://dx.doi.org/10.1016/j.compchemeng.2009.01.011.

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50

Hasebe, Shinji, Taketoshi Kurooka, Kei Higashimae, and Iori Hashimoto. "Selection of Optimal Structure of Batch Distillation System." KAGAKU KOGAKU RONBUNSHU 22, no. 6 (1996): 1351–58. http://dx.doi.org/10.1252/kakoronbunshu.22.1351.

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