Skip to content
Licensed Unlicensed Requires Authentication Published online by De Gruyter August 17, 2021

A survey on fractionation: the optimal control of distilling in batch and semibatch configurations

Marija Stojkovic EMAIL logo

Abstract

Since the middle of the last century, discussion about the operation of discontinuous fractionation to meet multifarious goals, such as product purity and recovery rate, by monitoring process variables including reflux or/and heat duty, is been on. The engineering practice showed intolerable events to occur; hereof the operation must be supervised, which makes it difficult to be in agreement with the batch distillation objectives. Hence, to uphold the effectuation of new operating policies into the industrial “know-how” techniques, different optimal control strategies can be conceived. The objective of this work is to offer a literature survey on the investigations of optimal control functioning for selected simple distillation column configurations employed in batch/semibatch distillation of homogeneous/reactive mixtures, as well as the approaches used in this regard. Available optimal control schemes have been reviewed in detail, emphasizing its major assets.


Corresponding author: Marija Stojkovic, Impasse de Copenhague 10, 53100Mayenne, France, E-mail:

  1. Author contributions: All the authors have accepted responsibility for the entire content of this submitted manuscript and approved submission.

  2. Research funding: None declared.

  3. Conflict of interest statement: The authors declare no conflicts of interest regarding this article.

References

Adams, T.A. and Seider, W.D. (2008). Semicontinuous distillation for ethyl lactate production. AIChE J. 54: 2539–2552, https://doi.org/10.1002/aic.11585.Search in Google Scholar

Akkaravathasinp, S., Narataruksa, P., and Prapainainar, C. (2015). The effect of feed location of a semi-batch reactive distillation via esterification reaction of acetic acid and methanol: simulation study. Energy Procedia 79: 778–783, https://doi.org/10.1016/j.egypro.2015.11.566.Search in Google Scholar

Albet, J. (1992). Rigorous simulation of multicomponent multisequence batch distillation. Toulouse: Thèse de Doctorat. Institut National Polytechnique.Search in Google Scholar

Arellano-Garcia, H., Carmona, I., and Wozny, G. (2008). New operational mode for reactive batch distillation in middle vessel columns: start-up and operation. Comp. Aid. Chem. Eng. 32: 161–169, https://doi.org/10.1016/j.compchemeng.2007.08.002.Search in Google Scholar

Aurangzeb, M. and Jana, A.K. (2018). Pressure-swing dividing-wall column with multiple binary azeotropes: improving energy efficiency and cost savings through vapor recompression. Ind. Eng. Chem. Res. 57: 4019–4032, https://doi.org/10.1021/acs.iecr.7b03586.Search in Google Scholar

Aurangzeb, M. and Jana, A.K. (2019). Vapor recompression with interreboiler in a ternary dividing wall column: improving energy efficiency and savings, and economic performance. Appl. Therm. Eng. 147: 1009–1023, https://doi.org/10.1016/j.applthermaleng.2018.11.008.Search in Google Scholar

Aqar, D.Y., Abass, A.S., Patel, R., and Mujtaba, I.M.. (2021 in press). Optimisation of semi-batch reactive distillation column for the synthesis of methyl palmitate. Sep. Purif. Technol. 270: 1187766, https://doi.org/10.1016/j.seppur.2021.118776.Search in Google Scholar

Aqar, D.Y. and Mujtaba, I.M. (2021). Economic feasibility of an integrated semi-batch reactive distillation operation for the production of methyl-decanoate. Separ. Purif. Technol. 257: 117871, https://doi.org/10.1016/j.seppur.2020.117871.Search in Google Scholar

Aqar, D.Y., Rahmanian, N., and Mujtaba, I.M. (2016a). Methyl lactate synthesis using batch reactive distillation: operational challenges and strategy for enhanced performance. Separ. Purif. Tehnol. 158: 193–203, https://doi.org/10.1016/j.seppur.2015.12.023.Search in Google Scholar

Aqar, D.Y., Rahmanian, N., and Mujtaba, I.M. (2016b). Integrated batch reactive distillation column configuration for optimal synthesis of methyl lactate. Chem. Eng. Process. Process. Intensification 108: 197–211, https://doi.org/10.1016/j.cep.2016.07.009.Search in Google Scholar

Aqar, D.Y., Rahmanian, N., and Mujtaba, I.M. (2017a). Significant profitability improvement for methyl-decanoate production using different types of batch distillation columns. Chem. Eng. Trans. 57: 1075–1080.Search in Google Scholar

Aqar, D.Y., Rahmanian, N., and Mujtaba, I.M. (2017b). Synthesis of methyl-decanoate using different types of batch reactive distillation systems. Ind. Eng. Chem. Res. 56: 3969–3982, https://doi.org/10.1021/acs.iecr.6b04255.Search in Google Scholar

Aqar, D.Y., Rahmanian, N., Edreder, E., Emtir, M., and Mujtaba, I.M. (2017c). Exploitation of integrated batch reactive distillation columns for number of chemical reaction systems. In: Fifth international conference of chemical engineering ICChE 2017, process modelling safety and control, Dhaka. ICChE 2017, pp. 895–900.Search in Google Scholar

Aqar, D.Y., Rahmanian, N., and Mujtaba, I.M. (2018). Investigation about profitability improvement for synthesis of benzyl acetate in different types of batch distillation columns. Chem. Eng. Trans. 70: 541–546.Search in Google Scholar

Aqar, D.Y., Rahmanian, N., and Mujtaba, I.M. (2019a). A novel split-reflux policy in batch reactive distillation for the optimal synthesis of a number of methyl esters. Separ. Purif. Technol. 221: 363–377, https://doi.org/10.1016/j.seppur.2019.03.071.Search in Google Scholar

Aqar, D.Y., Rahmanian, N., and Mujtaba, I.M. (2019b). The investigation of purity improvement for the production of methyl propionate in different types of batch distillation systems. Int. J. Oil Gas Coal Technol. 5: 68–81.Search in Google Scholar

Babu, G.U.B., Pal, E.K., and Jana, A.K. (2012a). An adaptive vapor recompression scheme for a ternary batch distillation with a side withdrawal. Ind. Eng. Chem. Res. 51: 4990–4997, https://doi.org/10.1021/ie201413p.Search in Google Scholar

Babu, G.U.B., Aditiya, R., and Jana, K. (2012b). Economic feasibility of novel energy efficient middle vessel batch distillation to reduce energy use. Energy 45: 626–633, https://doi.org/10.1016/j.energy.2012.07.035.Search in Google Scholar

Barakat, T.M., Fraga, E.S., and Sorensen, E. (2006). Multi-objective optimization of batch distillation processes. Comp. Aid. Chem. Eng. 21: 955–960, https://doi.org/10.1016/s1570-7946(06)80169-0.Search in Google Scholar

Barolo, M., Guarise, G.B., Ribon, N., Rienzi, S., Torota, A., and Macchietto, S. (1996). Some issues in the design and operation of batch distillation column with a middle vessel. Comp. Aid. Chem. Eng. 20: 37–42, https://doi.org/10.1016/0098-1354(96)00017-8.Search in Google Scholar

Barreto, A.A., Rodrigruez-Donis, I., Gerbaud, V., and Joulia, X. (2011a). Multi-objective optimization of three-phase batch extractive distillation. Comp. Aid. Chem. Eng. 29: 562–566, https://doi.org/10.1016/b978-0-444-53711-9.50113-9.Search in Google Scholar

Barreto, A.A., Rodrigruez-Donis, I., Gerbaud, V., and Joulia, X. (2011b). Optimization of heterogeneous batch extractive distillation. Ind. Eng. Chem. Res. 50: 5204–5217, https://doi.org/10.1021/ie101965f.Search in Google Scholar

Bernot, C., Doherty, M.F., and Malone, M.F. (1993). Design and operating targets for nonideal multicomponent batch distillation. Ind. Eng. Chem. Res. 32: 293–301, https://doi.org/10.1021/ie00014a008.Search in Google Scholar

Betlem, B.H.L., Krijnsen, H.C., and Huijnen, H. (1998). Optimal batch control based on specific measures. Chem. Eng. J. 71: 111–126, https://doi.org/10.1016/s1385-8947(98)00118-1.Search in Google Scholar

Bhatia, T. and Biegler, L.T. (1996). Dynamic optimization in the design and scheduling of multiproduct batch plants. Ind. Eng. Chem. Res. 35: 2234–2246, https://doi.org/10.1021/ie950701i.Search in Google Scholar

Bonny, L. (2006). Multicomponent batch distillation campaign: control variables and optimal recycling policy. Ind. Eng. Chem. Res. 45: 8998–9009, https://doi.org/10.1021/ie0609057.Search in Google Scholar

Bonny, L. (2013). Multicomponent batch distillation campaign: control variables and optimal recycling policy. A further note. Ind. Eng. Chem. Res. 52: 2190–2193, https://doi.org/10.1021/ie3018302.Search in Google Scholar

Bonny, L., Domenech, S., Floquet, P., and Pibouleau, L. (1994a). Strategies for slop-cut recycling in multicomponent batch distillation. Chem. Eng. Process 33: 23–31, https://doi.org/10.1016/0255-2701(94)87003-9.Search in Google Scholar

Bonny, L., Domenech, S., Floquet, P., and Pibouleau, L. (1994b). Recycling of a slop-cuts in multicomponent batch distillation. Comp. Aid. Chem. Eng. 18: 75–79, https://doi.org/10.1016/0098-1354(94)80013-8.Search in Google Scholar

Bonny, L., Domenech, S., Floquet, P., and Pibouleau, L. (1996). Optimal strategies for a batch distillation campaign of different mixtures. Chem. Eng. Process 35: 349–361, https://doi.org/10.1016/0255-2701(96)80015-8.Search in Google Scholar

Bosse, T. and Griewank, A. (2014). Optimal control of beer fermentation process with Lipschitz-contraint on the control. J. Inst. Brew. 120: 444–458.Search in Google Scholar

Bruggemann, S., Oldenburg, J., Zhang, P., and Marquardt, W. (2004). Robust dynamic simulation of three-phase reactive batch distillation columns. Ind. Eng. Chem. Res. 43: 3672–3684, https://doi.org/10.1021/ie034045v.Search in Google Scholar

Ceylan, H. and Ozgen, C. (2008). Dynamic modelling and optimal control of multicomponent batch distillation column. IFAC-PapersOnLine 41: 4548–4553, https://doi.org/10.3182/20080706-5-kr-1001.00765.Search in Google Scholar

Chiotti, O.J. and Iribarren, O.A. (1991). Simplified models for binary batch distillation. Comp. Aid. Chem. Eng. 15: 1–5, https://doi.org/10.1016/0098-1354(91)87001-p.Search in Google Scholar

Chiotti, O.J., Iribarren, O.A., and Salomone, H.E. (1993). Selection of multicomponent batch distillation sequences. Chem. Eng. Commun. 119: 1–21, https://doi.org/10.1080/00986449308936104.Search in Google Scholar

Christensen, F.M. and Jorgensen, S.B. (1987). Optimal control of binary batch distillation with recycled waste cut. Chem. Eng. J. 34: 57–64, https://doi.org/10.1016/0300-9467(87)87001-6.Search in Google Scholar

Chu, Y. and You, F. (2003). Integration of scheduling of batch processes under uncertainty: two-stage stochastic programming approach and enhanced generalized benders decomposition algorithm. Ind. Eng. Chem. Res. 52: 16851–16869.10.1021/ie402621tSearch in Google Scholar

Ciornei, C., Bumbac, G., Plesu, V., and Lavric, V. (2006). Modeling and simulation of a fedbatch reactive rectifier. In: CHISA 2006 proceedings, Vol. 6, p. 59.Search in Google Scholar

Converse, A.O. and Gross, G.D. (1963). Optimal distillate-rate policy in a batch distillation. IEC Fund 2: 217, https://doi.org/10.1021/i160007a010.Search in Google Scholar

Cortes-Garcia, G.E., Schaaf, J., and Kiss, A.A. (2017). A review on process intensification in HiGee distillation. Chem. Technol. Biotechol. 92: 1136–1156, https://doi.org/10.1002/jctb.5206.Search in Google Scholar

Coward, I. (1967). The time-optimal problem in a binary batch distillation. Chem. Eng. Sci. 22: 503, https://doi.org/10.1016/0009-2509(67)80033-2.Search in Google Scholar

Cuille, P.E. and Reklaitis, G.V. (1986). Dynamic simulation of multicomponent batch rectification with chemical reaction. Comp. Aid. Chem. Eng. 10: 339–398, https://doi.org/10.1016/0098-1354(86)87009-0.Search in Google Scholar

Dai, W., Word, D.P., and Hahn, J. (2014). Modeling and dynamic optimization of fuel-grade ethanol fermentation using fed-batch process. Contr. Eng. Pract. 22: 231–241, https://doi.org/10.1016/j.conengprac.2013.01.005.Search in Google Scholar

Dandekar, P. and Doherty, M.F. (2014). A mechanistic growth model for inorganic crystals: growth mechanism. AIChE J. 60: 3720–3731, https://doi.org/10.1002/aic.14513.Search in Google Scholar

Dandekar, P., Kuadia, Z.B., and Doherty, M.F. (2013). Engineering crystal morphology. Annu. Rev. Mater. Res. 43: 359–386, https://doi.org/10.1146/annurev-matsci-071312-121623.Search in Google Scholar

Demartzis, T. and Seferlis, P. (2010). Optimal design of staged three-phase reactive distillation columns using nonequilibrium and orthogonal collocation methods. Ind. Eng. Chem. Res. 49: 3275–3285.10.1021/ie901260bSearch in Google Scholar

Diehl, M., Schafer, A., Bock, H.G., Schloder, J.P., and Leineweber, D.B. (2002). Optimization of multiple-fraction batch distillation with recycled waste cuts. AIChE J. 48: 2869–2874, https://doi.org/10.1002/aic.690481214.Search in Google Scholar

Diwekar, U.M. (1992). Unified approach to solving optimal design control problems in batch distillation. AIChE J. 38: 1571, https://doi.org/10.1002/aic.690381007.Search in Google Scholar

Diwekar, U.M. (1994). Batch distillation: simulation, design, and optimal control. Taylor and Francis.Search in Google Scholar

Diwekar, U.M. (2014). Batch processing: modelling and design. Boca Raton: CRC Press.10.1201/b16527Search in Google Scholar

Diwekar, U.M. and Madhavan, K.P. (1989). Optimization of multicomponent batch distillation columns. Ind. Eng. Chem. Res. 28: 1011–1017, https://doi.org/10.1021/ie00091a019.Search in Google Scholar

Diwekar, U.M. and Rivier, C. (2019). Missing components in multicomponent batch distillation and optimal control. Ind. Eng. Chem. Res. 58: 17455–17461, https://doi.org/10.1021/acs.iecr.9b02242.Search in Google Scholar

Diwekar, U.M., Malik, R.K., and Madhavan, K.P. (1987). Optimal reflux rate policy determination for multicomponent batch distillation columns. Comp. Aid. Chem. Eng. 11: 629–637, https://doi.org/10.1016/0098-1354(87)87008-4.Search in Google Scholar

Doherty, M.F. and Malone, M.F. (2001). Conceptual design of distillation systems. New York: McGraw Hill, pp. 670.Search in Google Scholar

Domenech, S. and Enjalbert, M. (1981). Program for simulation batch rectification as unit operation. Comput. Chem. Eng. 5: 181–184, https://doi.org/10.1016/0098-1354(81)85007-7.Search in Google Scholar

Edreder, E.A., Mujtaba, I.M., and Emtir, M. (2013). Comparison of Conventional and Middle Vessel Batch Reactive Distillation Column: Application to Hydrolysis of Methyl Lactate to Lactic Acid. Chem. Eng. Trans. 35, https:// 10.3303/CET1335154.Search in Google Scholar

Edreder, E.A., Emtir, M.M., and Mujtaba, I.M. (2008a). Dynamic optimization of semi-batch reactive distillation column. In: Proceedings of the international conference in chemical engineering, Dhaka. ICChE 2008.Search in Google Scholar

Edreder, E.A., Emtir, M.M., and Mujtaba, I.M. (2008b). Improving the maximal conversion of ethanol esterification. Chem. Prod. Process Model. 3: 36, https://doi.org/10.2202/1934-2659.1208.Search in Google Scholar

Edreder, E.A., Emtir, M.M., and Mujtaba, I.M. (2009a). Profitability analysis for batch reactive distillation process based on fixed product demand. Chem. Eng. Trans. 18: 701–706.Search in Google Scholar

Edreder, E.A., Emtir, M.M., and Mujtaba, I.M. (2009b). Optimisation of design operation and scheduling of batch reactive distillation process with strict product specifications and fixed product demands using gPROMS. Comp. Aid. Chem. Eng. 26: 411–415, https://doi.org/10.1016/s1570-7946(09)70069-0.Search in Google Scholar

Edreder, E.A., Emtir, M.M., and Mujtaba, I.M. (2010). Improving the maximum productivity for ethyl acetate synthesis using gPROMS. Chem. Eng. Trans. 21: 901–906.Search in Google Scholar

Edreder, E.A., Emtir, M.M., and Mujtaba, I.M. (2011). Optimal operations of different types of batch reactive distillation columns used for hydrolysis of methyl lactate to lactic acid. Chem. Eng. J. 172: 467–475, https://doi.org/10.1016/j.cej.2011.06.027.Search in Google Scholar

Edreder, E.A., Emtir, M.M., and Mujtaba, I.M. (2012). Simulation of a middle vessel batch reactive distillation column: application to hydrolysis of methyl acetate. Chem. Eng. Trans. 29: 595–600.Search in Google Scholar

Edreder, E.A., Emtir, M., and Mujtaba, I.M. (2014). Energy saving in conventional and unconventional batch reactive distillation: application to hydrolysis of methyl lactate system. Comp. Aid. Chem. Eng. 33: 1261–1266, https://doi.org/10.1016/b978-0-444-63455-9.50045-3.Search in Google Scholar

Edreder, E.A., Mujtaba, I.M., and Emtir, M. (2015). Optimal operation of batch reactive distillation process involving esterification reaction system. Chem. Eng. Trans. 172: 467–475.10.1016/j.cej.2011.06.027Search in Google Scholar

Egger, T., Egger, L.S., and Fieg, G. (2018). Scale and causes of catalytic activity loss in enzymatic catalyzed reactive distillation. Chem. Eng. Sci. 178: 324–334, https://doi.org/10.1016/j.ces.2017.12.050.Search in Google Scholar

Egly, H., Ruby, V., and Sied, B. (1979). Optimum design and operation of batch rectification accompanied by chemical reaction. Comp. Aid. Chem. Eng. 3: 169–174, https://doi.org/10.1016/0098-1354(79)80028-9.Search in Google Scholar

Elgue, S., Prat, L., Cabassud, M., Le Lann, J.M., and Cézarec, J. (2002). Optimization of a methyl acetate production process by reactive batch distillation. Comp. Chem. Aid. Eng. 10: 475–480, https://doi.org/10.1016/s1570-7946(02)80107-9.Search in Google Scholar

Ely, T.O., Kambazek, D., and Chakraborty, D. (2019 in press). Batteries safety: recent progress and current challenges. Front. Energy Res.: 7–71, https://doi.org/10.3389/fenrg.2019.00071.Search in Google Scholar

Farhat, S., Pibouleau, L., Domenech, S., and Czernicki, M. (1991). Optimal control of batch distillation via nonlinear programming. Chem. Eng. Process. 29: 33–38.10.1016/0255-2701(91)87004-MSearch in Google Scholar

Farmer, T.C., Eric, W.M., and Doherty, M.F. (2019). Membrane bubble column reactor model for the production of hydrogen by methane pyrolysis. Int. J. Hydrog. Energy 44: 14721–14731, https://doi.org/10.1016/j.ijhydene.2019.03.023.Search in Google Scholar

Farsi, A., Kayhan, O., Chehade, G., Dincer, I., and Natarer, G.F. (2020). Multiphase flow model and experimental study of pressure-swing distillation for low pressure process of hydrochloric/water separation in hydrogen production. Comp. Aid. Chem. Eng. 141: 107020, https://doi.org/10.1016/j.compchemeng.2020.107020.Search in Google Scholar

Fernholz, G., Engell, S., Kreul, L.U., and Gorak, A. (2000). Optimal operation of a semi-batch reactive distillation column. Comp. Aid. Chem. Eng. 24: 1569–1575, https://doi.org/10.1016/s0098-1354(00)00553-6.Search in Google Scholar

Fonseka, J.D., Latifi, A.M., Orjuela, A., Rodriguez, G., and Gil, I.D. (2020). Modeling, analysis, and multi-objective optimization of an industrial batch process for the production of tributyl citrate. Comp. Aid. Chem. Eng. 132: 106603.10.1016/j.compchemeng.2019.106603Search in Google Scholar

Furlonge, H.I., Pantelidas, C.C., and Sorensen, E. (1999). Optimal operation of multivessel batch distillation columns. AIChE J. 45: 781–801, https://doi.org/10.1002/aic.690450413.Search in Google Scholar

Galindez, H. and Fredenslund, A. (1988). Simulation of multicomponent batch distillation process. Comp. Aid. Chem. Eng. 12: 2081–2088, https://doi.org/10.1016/0098-1354(88)85039-7.Search in Google Scholar

Greaves, M.A., Mujtaba, I.M., Barolo, M., Trotta, A., and Hussain, M.A. (2003). Neural-network approach to dynamic optimization of batch distillation: application to a middle-vessel column. Chem. Eng. Res. Des. 81: 393–401, https://doi.org/10.1205/02638760360596946.Search in Google Scholar

Griffiths, S., Pimputkar, S., Kearns, J., Malkowski, T.F., Doherty, M.F., Speck, J.S., and Nakamura, S. (2018). Growth kinetics of of basic ammonothermal gallium nitride crystals. J. Cryst. Growth 501: 74–80, https://doi.org/10.1016/j.jcrysgro.2018.08.028.Search in Google Scholar

Hanke, M. and Li, P. (2000). Simulated annealing for the optimization of batch distillation processes. Comp. Aid. Chem. Eng. 24: 1–8, https://doi.org/10.1016/s0098-1354(00)00317-3.Search in Google Scholar

Hansen, T.T. and Jorgensen, S.B. (1986). Optimal control of binary batch distillation in tray or packed columns. Chem. Eng. J. 33: 151–155, https://doi.org/10.1016/0300-9467(86)80014-4.Search in Google Scholar

Hasebe, S., Aziz, B.B.A., Hashimoto, I., and Watanabe, T. (1992). Optimal design and operation of complex batch distillation column. In: Interactions between process design and process control. Pergamon, pp. 177–182.10.1016/B978-0-08-042063-9.50026-1Search in Google Scholar

Hussain, A., Chaniago, Y.D., Riaz, A., and Lee, M. (2019a). Significance of operating pressure on process intensification in a distillation with side reactor configuration. Separ. Purif. Technol. 213: 533–544, https://doi.org/10.1016/j.seppur.2018.12.065.Search in Google Scholar

Hussain, A., Chaniago, Y.D., Riaz, A., and Lee, M. (2019b). Design method for the feasibility and technical evaluation of side reactor column configuration. Chem. Eng. Process Process Intensification 144: 107648, https://doi.org/10.1016/j.cep.2019.107648.Search in Google Scholar

Jain, S., Kim, J.-K., and Smith, R. (2012). Operational optimization of batch distillation systems. Ind. Eng. Chem. Res. 51: 5749–5761, https://doi.org/10.1021/ie201844g.Search in Google Scholar

Jana, A.K. (2014). Advances in heat pump assisted distillation column: a review. Energy Convers. Manag. 77: 287–297, https://doi.org/10.1016/j.enconman.2013.09.055.Search in Google Scholar

Jana, A.K. (2016a). A new divided-wall heat integrated distillation column (HIDiC) for batch processing: feasibility and analysis. Appl. Energy 172: 199–206, https://doi.org/10.1016/j.apenergy.2016.03.117.Search in Google Scholar

Jana, A.K. (2016b). Dynamic simulation, numerical control, and analysis of a novel bottom flashing scheme on batch distillation. Comp. Aid. Chem. Eng. 89: 166–171, https://doi.org/10.1016/j.compchemeng.2016.04.010.Search in Google Scholar

Jana, A.K. (2017a). A thermally coupled dividing tower batch rectifier: energy consumption and cost. Appl. Therm. Eng. 119: 610–616, https://doi.org/10.1016/j.applthermaleng.2017.03.076.Search in Google Scholar

Jana, A.K. (2017b). An energy efficient middle vessel batch distillation: techno-economic feasibility, dynamics, and control. Appl. Therm. Eng. 123: 411–421, https://doi.org/10.1016/j.applthermaleng.2017.05.106.Search in Google Scholar

Jana, A.K. (2019). Performance analysis of a heat integrated column with heat pumping. Separ. Purif. Technol. 209: 18–25, https://doi.org/10.1016/j.seppur.2018.07.011.Search in Google Scholar

Jana, A.K. and Debadrita, M. (2013). An ideal internally heat integrated batch distillation with a jacketed still with application to a reactive system. Energy 57: 527–534, https://doi.org/10.1016/j.energy.2013.05.014.Search in Google Scholar

Jana, A.K. and Maiti, D. (2013). Assessment of the implementation of vapor recompression technique in batch distillation. Separ. Purif. Technol. 107: 1–10, https://doi.org/10.1016/j.seppur.2013.01.018.Search in Google Scholar

Jana, A.K., Khan, M.M.N., and Maiti, D. (2013). Improving energy-efficiency and cost-effectiveness of batch distillation for separating wide boiling constituents II: internal versus external heat integration. Chem. Eng. Process Process Intensfication 72: 122–129, https://doi.org/10.1016/j.cep.2013.08.002.Search in Google Scholar

Jang, S.-S. (1993). Dynamic optimization of multicomponent batch distillation processes using continuous and discontinuous collocation polynomial policies. Chem. Eng. J. 51: 83–92, https://doi.org/10.1016/0300-9467(93)80014-f.Search in Google Scholar

Johri, K., Babu, G.U.B., and Jana, A.K. (2011). Performance investigation of a variable speed vapor recompression reactive batch rectifier. AIChE J. 57: 3238–3242, https://doi.org/10.1002/aic.12546.Search in Google Scholar

Joswiak, M.N., Doherty, M.F., and Peters, B. (2018). Ion dissolution mechanism and kinetics at kink cites on NaCl surfaces. Proc. Natl. Acad. Sci. USA 115: 656–661, https://doi.org/10.1073/pnas.1713452115.Search in Google Scholar

Kao, Y.L. and Ward, J.D. (2014a). Design and optimization of batch reactive distillation processes with off-cut. J. Taiw. Inst. Chem. Eng. 45: 411–420, https://doi.org/10.1016/j.jtice.2013.05.018.Search in Google Scholar

Kao, Y.L. and Ward, J.D. (2014b). Improving batch reactive distillation process with off-cut. Ind. Eng. Chem. Res. 53: 8528–8542, https://doi.org/10.1021/ie404229w.Search in Google Scholar

Kao, Y.L. and Ward, J.D. (2015). Batch reactive distillation with off-cut recycling. Ind. Eng. Chem. Res. 54: 2188–2200, https://doi.org/10.1021/ie5042929.Search in Google Scholar

Kao, Y.L. and Ward, J.D. (2016). Simultaneous optimization of the design and operation of batch reactive distillation processes. Ind. Eng. Chem. Res. 55: 267–278, https://doi.org/10.1021/acs.iecr.5b03170.Search in Google Scholar

Keith, F.M. and Brunet, J.D. (1971). Optimal operation of a batch packed distillation columns. Can. J. Chem. Eng. 41: 291, https://doi.org/10.1002/cjce.5450490222.Search in Google Scholar

Kerkhof, L.H. and Vissers, H.J.M. (1978). On the profit of optimum control in batch distillation. Chem. Eng. Sci. 33: 961–970, https://doi.org/10.1016/0009-2509(78)85187-2.Search in Google Scholar

Khan, M.M.N., Babu, G.U.B., and Jana, A.K. (2012). Improving energy efficiency and cost-effectiveness of batch distillation for separating wide boiling constituents. 1. Vapor recompression column. Ind. Eng. Chem. Res. 51: 15413–15422, https://doi.org/10.1021/ie300907b.Search in Google Scholar

Kim, K.J. and Diwekar, U.M. (2001a). Entrainer selection and solvent recycling in complex batch distillation. Chem. Eng. Commun. 191: 1606–1633.10.1080/00986440490472724Search in Google Scholar

Kim, K.J. and Diwekar, U.M. (2001b). New era in batch distillation: computer aided analysis, optimal design and control. Rev. Chem. Eng. 17: 111–164, https://doi.org/10.1515/revce.2001.17.2.111.Search in Google Scholar

Kim, K.J. and Ju, D.P. (2003). Multicomponent batch distillation with distillate receiver. Kor. J. Chem. Eng. 20: 522–527, https://doi.org/10.1007/bf02705559.Search in Google Scholar

Kim, S.H., Dandekar, P., Lovette, M.A., and Doherty, M.F. (2014). Kink rate model for the general case of organic molecular crystals. Cryst. Growth Des. 14: 2460–2467, https://doi.org/10.1021/cg500167a.Search in Google Scholar

Klein, A. (2008). Azeotropic pressureswing distillation, PhD thesis. Berlin: Technical University Berlin, Faculty III- Science of Processes.Search in Google Scholar

Knott, B.C., LaRue, J.L., Wodtke, A.M., Doherty, M.F., and Mpeters, B. (2011). Communication: bubbles, crystals, and laser-induced nucleation. J. Chem. Phys. 134: 171102, https://doi.org/10.1063/1.3582897.Search in Google Scholar PubMed

Konakom, K., Saengchan, A., Kittisupakorn, P., and Mujtaba, I.M. (2010). High purity ethyl-acetate production with a batch reactive distillation column using dynamic optimization strategy for multi-objective dynamic optimization strategy. In: Proceedings of the world congress on engineering and computer science, pp. 20–22.Search in Google Scholar

Kim, K.J., and Diwekar, U. (2000). Comparing batch column configurations: parametric study involving multiple objectives. AIChE J. 46: 2475–2488, https://doi.org/10.1002/aic.690461214.Search in Google Scholar

Kumar, R. and Mahajani, S.M. (2007). Esterification of lactic acid with n-butanol by reactive distillation. Ind. Eng. Chem. Res. 46: 6873–6882, https://doi.org/10.1021/ie061274j.Search in Google Scholar

Landis, S., Yongsheng, Z., and Doherty, M.F. (2020). Digital design of crystalline solids. Comp. Aid. Chem. Eng. 133: 106637, https://doi.org/10.1016/j.compchemeng.2019.106637.Search in Google Scholar

Lee, M.J., Chou, P.L., and Lin, H.M. (2005). Kinetics of synthesis and hydrolysis of ethyl benzoate over Amberlyst 39. Ind. Eng. Chem. Res. 44: 725–732, https://doi.org/10.1021/ie049437w.Search in Google Scholar

Leipold, L., Gruetzmann, S., and Fieg, G. (2009). An revolutionary approach for multi-objective dynamic optimization applied to middle vessel batch column. Comp. Aid. Chem. Eng. 33: 857–870, https://doi.org/10.1016/j.compchemeng.2008.12.010.Search in Google Scholar

Li, P. and Wozny, G. (1997). Dynamische Optimierung großer chemischer Prozesse mit Kollokations – Verfahren am Beispiel Batch-Destillation. At-Automatisierungstechnik 145: 136–143, https://doi.org/10.1524/auto.1997.45.3.136.Search in Google Scholar

Li, P., Garcia, H.A., Wozny, G., and Reuter, E. (1998). Optimization of a semi-batch distillation process with model validation on an industrial site. Ind. Eng. Chem. Res. 37: 1341–1350, https://doi.org/10.1021/ie970695l.Search in Google Scholar

Li, J., Tilbury, C.J., Kim, S.H., and Doherty, M.F. (2016). A design aid for crystal growth engineering. Prog. Mater. Sci. 82: 1–38, https://doi.org/10.1016/j.pmatsci.2016.03.003.Search in Google Scholar

Li, X., Zhao, Y., Qin, B., Zhang, X., Wang, Y., and Zhu, Z. (2017). Optimization of pressure-swing batch distillation with and without heat integration for separating dichloromethane/methanol azerotrope based on minimum total annual cost. Ind. Eng. Chem. Res. 14: 4104–4112, https://doi.org/10.1021/acs.iecr.7b00464.Search in Google Scholar

Loeblein, C., Perkins, J.D., Shrinivasan, B., and Bonvin, D. (1997). Performance analysis of on-line batch optimization systems. Comp. Aid. Chem. Engng. 21: 867–872.Search in Google Scholar

Logsdon, J.S. and Biegler, L.T. (1989). Accurate solution of differential-algebraic optimization problems. Ind. Eng. Chem. Res. 28: 1628–1639, https://doi.org/10.1021/ie00095a010.Search in Google Scholar

Logsdon, J.S. and Biegler, L.T. (1993). Accurate determination of optimal reflux policies for the maximum distillate problem in batch distillation. Ind. Eng. Chem. Res. 32: 692–700, https://doi.org/10.1021/ie00016a016.Search in Google Scholar

Logsdon, J.S., Diwekar, U.M., and Biegler, L.T. (1990). On the simultaneous optimal design and operation of distillation columns. Chem. Eng. Res. Des. 68: 434–444.Search in Google Scholar

Lopez-Saucedo, E.S., Grossmann, I.E., Segovia-Hernandez, J.G., and Hernández, S. (2016). Rigorous modeling, simulation, and optimization of a conventional and nonconventional batch reactive distillation column: a comparative study of dynamic optimization approaches. Chem. Eng. Res. Des. 111: 83–99, https://doi.org/10.1016/j.cherd.2016.04.005.Search in Google Scholar

Lovette, M.A., Browning, A.R., Griffin, D.W., Sizemore, J.P., Snyder, R.C., and Doherty, M.F. (2008). Crystal shape engineering. Ind. Eng. Chem. Res. 47: 9812–9833, https://doi.org/10.1021/ie800900f.Search in Google Scholar

Lovette, M.A., Muratore, M., and Doherty, M.F. (2012). Crystal shape modification through cycles of dissolution and growth: attainable regions and experimental validation. AIChE J. 58: 1465–1474, https://doi.org/10.1002/aic.12707.Search in Google Scholar

Low, K.H. and Sorensen, E. (2003). Simultaneous optimal design and operation of multivessel batch distillation. AIChE J. 49: 2563–2576, https://doi.org/10.1002/aic.690491011.Search in Google Scholar

Low, K.H. and Sorensen, E. (2004). Simultaneous optimal design and operation of multipurpose batch distillation columns. Chem. Eng. Process. 43: 273–289, https://doi.org/10.1016/s0255-2701(03)00123-5.Search in Google Scholar

Low, K.H., and Sorensen, E. (2005). Simultaneous optimal configuration, design and operation of batch distillation. AIChE J 51: 1700–1713, https://doi.org/10.1002/aic.10522.Search in Google Scholar

Luna, R., López, F., and Pérez-Correa, J.R. (2021). Design of optimal wine distillation recipes using multi-criteria decision-making techniques. Comp. Aid. Chem. Eng. 145: 107194, https://doi.org/10.1016/j.compchemeng.2020.107194.Search in Google Scholar

Luyben, W.L. (1971). Some practical aspects of optimal batch distillation design. IEC PDD 10: 54–59, https://doi.org/10.1021/i260037a010.Search in Google Scholar

Luyben, W.L. (1988). Multicomponent batch distillation I. Ternary systems with slop recycle. Ind. Eng. Chem. Res. 27: 642–647, https://doi.org/10.1021/ie00076a019.Search in Google Scholar

Madabhushi, P.B. and Adams, T.A.II (2018). Side stream control in semicontinuous distillation. Comp. Aid. Chem. Eng. 119: 450–464, https://doi.org/10.1016/j.compchemeng.2018.09.002.Search in Google Scholar

Maher, R.A. (2013). Optimal control engineering with MATLAB. New York: NOVA Science Publishers, pp. 422.Search in Google Scholar

Masoud, A.Z. and Mujtaba, I.M. (2009). Effect of operating decisions on the design and energy consumption of inverted batch distillation column. Chem. Prod. Process Model. 4: 1–10, https://doi.org/10.2202/1934-2659.1275.Search in Google Scholar

Mayur, D.N. and Jackson, R. (1971). Time optimal control problems in batch distillation for multicomponent mixtures and for columns with holdup. Chem. Eng. J. 2: 150–163, https://doi.org/10.1016/0300-9467(71)80012-6.Search in Google Scholar

Mayur, D.N., May, R., and Jackson, R. (1970). The time-optimal problem in binary batch distillation with a recycled waste-cut. Chem. Eng. J. 1: 15–21, https://doi.org/10.1016/0300-9467(70)85026-2.Search in Google Scholar

Meidanshahi, V. (2016). Advances in design, optimization and control of semicontinuous distillation processes, PhD thesis. Ontario, Canada: McMaser University.Search in Google Scholar

Merger, J., Borzi, A., and Herzog, R. (2017). Optimal control of a system of reaction-diffusion equations modeling the wine fermentation process. Optim. Contr. Appl. Methods 38: 112–132, https://doi.org/10.1002/oca.2246.Search in Google Scholar

Miladi, M.M. and Mujtaba, I.M. (2004). Optimization of design and operation policies of binar batch batch distillation with fixed product demand. Comp. Aid. Chem. Eng. 28: 2377–2390, https://doi.org/10.1016/j.compchemeng.2004.06.001.Search in Google Scholar

Mujtaba, I.M. (1997). Use of continuous distillation columns for batch separations. Chem. Eng. Res. Des. 75: 609–619, https://doi.org/10.1205/026387697524137.Search in Google Scholar

Mujtaba, I.M. (2004). Batch distillation: design and operation. London: Imperial College Press.10.1142/p319Search in Google Scholar

Mujtaba, I.M. and Macchietto, S. (1988). Optimal control of batch distillation. In: Vichnevetsky, P. Borne and Vignes, J. (Eds.). Proceedings of 12th IMACS World Congress. IMACS, Paris, pp. 635.Search in Google Scholar

Mujtaba, I.M. and Macchietto, S. (1992). An optimal recycle policy for multicomponent batch distillation. Comp. Aid. Chem. Eng. 16: 273–280, https://doi.org/10.1016/s0098-1354(09)80032-x.Search in Google Scholar

Mujtaba, I.M. and Macchietto, S. (1993). Optimal operation of multicomponent batch distillations - multiperiod formulation and solution. Chem. Eng. 17: 1191–1207, https://doi.org/10.1016/0098-1354(93)80099-9.Search in Google Scholar

Mujtaba, I.M. and Macchietto, S. (1994). Optimal operation of multicomponent batch distillation. A comparative study using conventional and unconventional columns. In: Proceedings ADCHEM 94, Japan, Vol. 94, pp. 1191–1207.10.1016/B978-0-08-042229-9.50067-7Search in Google Scholar

Mujtaba, I.M. and Macchietto, S. (1996). Simultaneous optimization and operation of batch distillation column single and multiple duties. J. Process Contr. 6: 27–36, https://doi.org/10.1016/0959-1524(95)00028-3.Search in Google Scholar

Mujtaba, I.M., Edreder, E.A., and Emtir, M.M. (2012). Significant thermal energy reduction in lactic acid production. Appl. Energy 89: 74–80, https://doi.org/10.1016/j.apenergy.2010.11.031.Search in Google Scholar

Murty, B.S.N., Gangiah, K., and Husain, A. (1980). Performance of various methods in computing optimal control policies. Chem. Eng. J. 19: 201–208, https://doi.org/10.1016/0300-9467(80)80030-x.Search in Google Scholar

Mussati, M.C., Aguirre, P.A., Espinosa, J., and Iribarren, O.A. (2006). Optimal design of azeotropic batch distillation. AIChE J. 52: 968–985, https://doi.org/10.1002/aic.10696.Search in Google Scholar

Nad, L. and Speigel, L. (1987). Simulation of batch distillation by computer and comparison with experiment. In: The use of computers in chemical engineering. Sicily, Italy, p. 737.Search in Google Scholar

Nemeth, B., Lang, P., and Hegely, L. (2020). Optimization of solvent recovery in two batch distillation columns at of different size. J. Clean. Prod. 275: 122746, https://doi.org/10.1016/j.jclepro.2020.122746.Search in Google Scholar

Parhi, S.S., Rangaiah, G.P., and Jana, A.K. (2019a). Vapor recompressed batch distillation: optimizing reflux ration at variable mode. Comp. Aid. Chem. Eng. 124: 184–196, https://doi.org/10.1016/j.compchemeng.2019.02.014.Search in Google Scholar

Parhi, S.S., Rangaiah, G.P., and Jana, A.K. (2019b). Multi-objective optimization of vapor recompressed distillation column in batch distillation: improving energy and cost savings. Appl. Therm. Eng. 150: 1273–1296, https://doi.org/10.1016/j.applthermaleng.2019.01.073.Search in Google Scholar

Parhi, S.S., Rangaiah, G.P., and Jana, A.K. (2019c). Optimizing reboiler duty and reflux ratio profiles of vapor recompressed batch distillation. Separ. Purif. Technol. 213: 553–570, https://doi.org/10.1016/j.seppur.2018.12.066.Search in Google Scholar

Parhi, S.S., Rangaiah, G.P., and Jana, A.K. (2020). Mixed-Integer dynamic optimization of conventional and vapor recompressed batch distillation for economic and environmental objectives. Chem. Eng. Res. Des. 154: 75–80, https://doi.org/10.1016/j.cherd.2019.12.006.Search in Google Scholar

Phimister, J.R. and Seider, W.D. (2000). Semicontinuous pressure-swing distillation. Ind. Eng. Chem. Res. 39: 122–130, https://doi.org/10.1021/ie9904302.Search in Google Scholar

Pibouleau, L., Floquet, P., and Domenech, S. (1985). Optimisation des procédés chimiques par une méthode de gradient réduit partie I. Présentation d’algorithme. RAIRO, Recherche Oppérationelle 19: 247–274, https://doi.org/10.1051/ro/1985190302471.Search in Google Scholar

Pommier, S., Massebeuf, S., Kotai, B., Lang, P., Baudouin, O., Floquet, P., and Gerbaud, V. (2008). Heterogeneous batch distillation processes: real system optimization. Chem. Eng. Process Process Intensification 47: 408–419, https://doi.org/10.1016/j.cep.2007.01.022.Search in Google Scholar

Quintero-Marmol, E. and Luyben, W.L. (1990). Multicomponent batch distillation II. Comparison of alternative slop handling and and operating strategies. Ind. Eng. Chem. Res. 29: 1915–1921, https://doi.org/10.1021/ie00105a025.Search in Google Scholar

Raducan, O., Woinaroschu, A., and Lavric, V. (2005). Free time optimal control of a batch distillation column through genetic algorithms. Rev. Chim. 56: 1114–1119.Search in Google Scholar

Reddy, P.S., Rani, K.Y., and Pathwardhan, S.C. (2017a). Multu-objective optimization of a reactive batch distillation process using reduced order model. Comp. Aid. Chem. Eng. 106: 40–56, https://doi.org/10.1016/j.compchemeng.2017.05.017.Search in Google Scholar

Reddy, P.S., Rani, K.Y., and Patwardhan, S.C. (2017b). Multi-objective optimization of a batch reactive distillation process using reduced order model. Comp. Aid. Chem. Eng. 106: 40–56, https://doi.org/10.1016/j.compchemeng.2017.05.017.Search in Google Scholar

Repke, J.U., Klein, A., Bogle, D., and Wozny, G. (2007). Pressure swing batch distillation for homogeneous azeotropic separation. Chem. Eng. Res. Des. 85: 492–501, https://doi.org/10.1205/cherd06092.Search in Google Scholar

Robinson, E.R. (1969). The optimization of batch distillation operations. Chem. Eng. Sci. 24: 1661–1668, https://doi.org/10.1016/0009-2509(69)87031-4.Search in Google Scholar

Robinson, E.R. (1970). The optimal control of an industrial batch distillation column. Chem. Eng. Sci. 25: 921–928, https://doi.org/10.1016/0009-2509(70)85037-0.Search in Google Scholar

Robinson, C.S. and Gilliland, E.R. (1950). Elements of fractional distillation, 4th ed. McGraw Hill Book Company.Search in Google Scholar

Rodriguez-Donis, I., Hernandez-Gonzalez, N., Gerbaud, V., and Joulia, X. (2012). Thermodynamic efficiency and cost-effective optimization of heterogeneous batch distillation. Comp. Aid. Chem. Eng. 30: 362–366, https://doi.org/10.1016/b978-0-444-59519-5.50073-3.Search in Google Scholar

Safrit, B.T. and Westerberg, A. (1997). Improved operational policies for batch extractive distillation columns. Ind. Eng. Chem. Res. 36: 436–444, https://doi.org/10.1021/ie960343z.Search in Google Scholar

Schenk, C. and Schulz, V. (2015). Energy-optimal control of temperature for wine fermentation based on a novel model including the yeast dying phase. IFAC-PapersOnLine 48: 452–457, https://doi.org/10.1016/j.ifacol.2015.11.320.Search in Google Scholar

Shi, H. and You, F. (2015 in press). A novel adaptive surrogate modeling‐based algorithm for simultaneous optimization of sequential batch process scheduling and dynamic operations. AIChE J. 61: 4191–4209, https://doi.org/10.1002/aic.14974.Search in Google Scholar

Shrinivasan, B. and Bonvin, D. (2003). Convergence analysis of iterative identification and optimization schemes. Comp. Aid. Chem. Eng. 27: 27–44.Search in Google Scholar

Sorensen, E. (1999). A cyclic operating policy for batch distillation – theory and practice. Comp. Aid. Chem. Eng. 23: 533–542.10.1016/S0098-1354(98)00291-9Search in Google Scholar

Sorensen, E. and Prentzler, M. (1997). A cyclic operating policy for batch distillation – theory and practice. Comp. Aid. Chem. Eng. 21: 1215–1220.Search in Google Scholar

Sorensen, E. and Skogestad, S. (1994). Optimal operating policies of batch distillation with emphasis on the cyclic operating policy. In: Proceedings of PSE’94, pp. 449-456.Search in Google Scholar

Sorensen, E. and Skogestad, S. (1996). Optimal startup procedures for batch distillation. Comput. Chem. Eng. 20: 1257–1262.10.1016/0098-1354(96)00217-7Search in Google Scholar

Sorensen, E., Macchietto, S., Stuart, G., and Skogestad, S. (1996). Optimal control of reactive distillation. Comput. Chem. Eng. 20: 1491–1498.10.1016/0098-1354(95)00234-0Search in Google Scholar

Stojkovic, M. (2017). Contrôle optimal des procédés discontinus pour la séparation des mélanges non-idéaux. Toulouse: Thèse de Doctorat. Institut National Polytechnique.Search in Google Scholar

Stojkovic, M., Gerbaud, V., and Shcherbakova, N. (2017). Batch distillation of binary mixtures: preliminary analysis of optimal control. IFAC-PapersOnLine 50: 4899–4904, https://doi.org/10.1016/j.ifacol.2017.08.743.Search in Google Scholar

Stojkovic, M., Gerbaud, V., and Shcherbakova, N. (2018). Cyclic operation as optimal control reflux policy of binary mixture batch distillation. Comp. Aid. Chem. Eng. 108: 98–111, https://doi.org/10.1016/j.compchemeng.2017.09.004.Search in Google Scholar

Sun, Y., Tilbury, C.J., and Doherty, M.F. (2017). Modeling olanzapine solution growth morphologies. Cryst. Growth Des. 18: 905–911.10.1021/acs.cgd.7b01389Search in Google Scholar

Sundaram, S. and Evans, L.B. (1993). Synthesis of separations by batch distillation. Ind. Eng. Chem. Res. 32: 500–510, https://doi.org/10.1021/ie00015a013.Search in Google Scholar

Thotla, S. and Mahajani, S. (2009). Reactive distillation with side draw. Chem. Eng. Process: Process Intensification 48: 356–364, https://doi.org/10.1016/j.cep.2008.12.007.Search in Google Scholar

Tilbury, C.J. and Doherty, M.F. (2017). Modeling layered crystal growth at increasing supersaturation by connecting growth regimes. AIChE J. 63: 1338–1352, https://doi.org/10.1002/aic.15617.Search in Google Scholar

Tilbury, C.J., Joswiak, M.N., Peters, B., and Doherty, M.F. (2017). Modeling step velocities and edge surface structures during growth of non-centrosymmetric crystals. Cryst. Growth Des. 17: 2066–2080, https://doi.org/10.1021/acs.cgd.7b00058.Search in Google Scholar

Tricoire, B. and Malone, M.F. (1992). AIChE annual meeting: design of multiproduct batch processes for polymer production. Miami, FL.Search in Google Scholar

Ulas, S. (2003). Stochastic optimal control in batch distillation: a real options theory approach, PhD thesis. Chicago: University of Illinois.Search in Google Scholar

Ulas, S. and Diwekar, U.M. (2004). Thermodynamic uncertainties in batch processing and optimal control. Comp. Aid. Chem. Eng. 28: 2245–2258, https://doi.org/10.1016/j.compchemeng.2004.04.001.Search in Google Scholar

Ulas, S. and Diwekar, U.M. (2006). Integrating product and process design with optimal control: a case study of solvent recycling. Chem. Eng. Sci. 61: 2001–2009, https://doi.org/10.1016/j.ces.2005.10.033.Search in Google Scholar

Upreti, S.R. (2013). Optimal control for chemical engineers. Taylor & Francis.Search in Google Scholar

Varma, V.A., Reklaitis, G.V., Blau, G.E., and Pekny, J.F. (2007). Enterprise-wide modeling&optimization – an overview of emerging research challenges and opportunities. Comp. Aid. Chem. Eng. 31: 692–711, https://doi.org/10.1016/j.compchemeng.2006.11.007.Search in Google Scholar

Vassiliadis, V.S. (1992). DAEOPT – a differential algebraic optimal control problem solver, Version 1.0. In: Internal report. Imperial College.Search in Google Scholar

Venimadhavan, G., Malone, M.F., and Doherty, M.F. (1999). A novel distillate policy for batch reactive distillation with application to the production of the butyl acetate. Ind. Eng. Chem. Res. 38: 714–722, https://doi.org/10.1021/ie9804273.Search in Google Scholar

Vetter, T., Christopher, L.B., and Doherty, M.F. (2015a). Separation of conglomerate forming enantiomers using a novel continuous preferential crystallization process. AIChE J. 61: 2810–2823, https://doi.org/10.1002/aic.14934.Search in Google Scholar

Vetter, T., Christopher, L.B., and Doherty, M.F. (2015b). Designing robust crystallization processes in the presence of parameter uncertainty using attainable regions. Ind. Eng. Chem. Res. 54: 10350–10363, https://doi.org/10.1021/acs.iecr.5b00693.Search in Google Scholar

Wajge, R.G. and Reklaitis, G.V. (1999). RBDOPT: a general purpose object-oriented module for distribution campaign optimization of reactive distillation. Chem. Eng. J. 75: 57–68, https://doi.org/10.1016/s1385-8947(99)00020-0.Search in Google Scholar

Wang, Y., Yang, X., Liu, X., Yao, D., Cui, P., Wang, L., Zhu, Z., Li, X., and Xu, D. (2020). Design and comprehensive analysis of a novel pressure-swing batch distillation process for the separation of a binary azeotrope with various boiling behaviours. Separ. Purif. Technol. 251: 117329, https://doi.org/10.1016/j.seppur.2020.117329.Search in Google Scholar

Ward, J.D., Mellichamp, D.A., and Doherty, M.F. (2006). Choosing an operating policy for seeded batch crystallization. AIChE J. 52: 2046–2054, https://doi.org/10.1002/aic.10808.Search in Google Scholar

Ward, J.D., Yu, C.C., and Doherty, M.F. (2011). Analytical design operation of systems with crystallization, filtration and recycling. Ind. Eng. Chem. Res. 50: 1196–1205, https://doi.org/10.1021/ie901881u.Search in Google Scholar

Wierschem, M., Schlimper, M., Heils, R., Kiss, A.A., Skiborowski, M., and Lutze, P. (2017). Pilot-scale validation of enzymatic reactive distillation for butyl butyrate production. Chem. Eng. J. 312: 106–117, https://doi.org/10.1016/j.cej.2016.11.127.Search in Google Scholar

Wilson, J.A. (1987). Dynamic model based optimization in the design of batch processes involving simultaneous reaction and distillation. IChemE Symposium Series 100: 163, https://doi.org/10.1016/b978-0-85295-205-4.50018-9.Search in Google Scholar

Woinaroschy, A. and Isopescu, R. (2010). Time-optimal control of dividing-wall columns. Ind. Eng. Chem. Res. 49: 9195–9208, https://doi.org/10.1021/ie100090p.Search in Google Scholar

Zavala-Loria, J.C. and Coronado, C. (2008). Optimal control problem in batch distillation using thermodynamic efficiency. Ind. Eng. Chem. Res. 47: 2788–2793, https://doi.org/10.1021/ie0710972.Search in Google Scholar

Zavala-Loria, J.C., Ruiz-Marin, A., and Coronado-Velasco, C. (2011). Maximum thermodynamic efficiency problem in batch distillation. Braz. J. Chem. Eng. 28: 333–342, https://doi.org/10.1590/s0104-66322011000200018.Search in Google Scholar

Zhang, X., Jie, H., Zhang, W., Zhang, Z., Chungui, J., and Zhicai, Y. (2012). The operation of draining column holdup for slop-cut withdrawal in batch distillation. Chin. J. Chem. Eng. 14: 337–342.10.1016/S1004-9541(06)60080-3Search in Google Scholar

Zhang, X., Jie, H., Zhang, W., Zhang, Z., Chungui, J.I.A.N., and Zhical, J.A.N.G. (2006). The operation of draining column holdup for slop cut withdrawal in batch distillation. Chin. J. Chem. Eng. 14: 337–342, https://doi.org/10.1016/S1004-9541(06)60080-3.Search in Google Scholar

Received: 2021-01-27
Accepted: 2021-06-27
Published Online: 2021-08-17

© 2021 Walter de Gruyter GmbH, Berlin/Boston

Downloaded on 28.1.2023 from https://www.degruyter.com/document/doi/10.1515/revce-2021-0006/html
Scroll Up Arrow