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“Dynamics and Control of Distillation Columns - A Critical Survey”

Authors: Sigurd Skogestad,
Affiliation: NTNU, Department of Chemical Engineering
Reference: 1997, Vol 18, No 3, pp. 177-217.

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Keywords: Distillation, process control, process dynamics, control configuration, simulation, low-order model, literature review

Abstract: Distillation column dynamics and control have been viewed by many as a very mature or even dead field. However, as is discussed in this paper significant new results have appeared over the last 5-10 years. These results include multiple steady states and instability in simple columns with ideal thermodynamics (which was believed to be impossible), the understanding of the difference between various control configurations and the systematic transformation between these, the feasibility of using the distillate-bottom structure, for control (which was believed to be impossible), the importance of flow dynamics for control studies, the fundamental problems in identifying models from open-loops responses, the use of simple regression estimators to estimate composition from temperatures, and an improved general understanding of the dynamic behavior of distillation columns which includes a better understanding of the fundamental difference between internal and external flow, simple formulas for estimating the dominant time constant, and a derivation of the linearizing effect of logarithmic transformations. These issues apply to all columns, even for ideal mixtures and simple columns with only two products. In addition, there have been significant advances for cases with complex thermodynamics and complex column configurations. These include the behavior and control of azeotropic distillation columns, and the possible complex dynamics of nonideal mixtures and of interlinked columns. However, both for the simple and more complex cases there are still a number of areas where further research is needed.

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  [1] Andreas Linhart and Sigurd Skogestad (2010), doi:10.1016/j.ces.2010.02.032
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  [15] Weifeng Shen, Hassiba Benyounes and Vincent Gerbaud (2013), doi:10.1021/ie3011148
  [16] A. Téllez-Anguiano, F. Rivas-Cruz, C.-M. Astorga-Zaragoza, E. Alcorta-García and D. Juárez-Romero (2009), doi:10.1016/j.csi.2008.06.007
  [17] Francesco Corona, Michela Mulas, Roberto Baratti and Jose A. Romagnoli (2012), doi:10.1021/ie202854b
  [18] M. Diehl, R. Findeisen, S. Schwarzkopf, I. Uslu, F. Allgöwer, H. G. Bock, Ernst-Dieter Gilles and J. P. Schlöder (2003), doi:10.1524/auto.
  [19] Flavio Manenti (2012), doi:10.1016/j.isatra.2011.10.008
  [20] Anna Pulis, Carlos Fernandez, Roberto Baratti and Jesus Alvarez (2006), doi:10.1016/S1570-7946(06)80270-1
  [21] C. Defranoux, H. Garnier and P. Sibille (2000), doi:10.1002/1521-4125(200009)23:9<745::AID-CEAT745>3.0.CO;2-9
  [22] M. Schenk, R. Gani, D. Bogle and E.N. Pistikopoulos (1999), doi:10.1205/026387699526557
  [23] Vishal Mahindrakar and Juergen Hahn (2014), doi:10.1016/j.jprocont.2014.01.005
  [24] Lu Qiu, Yue Wang and Rolf D. Reitz (2014), doi:10.1002/aic.14519
  [25] Haotao Luo, Kai Liang, Weisong Li, Ye Li, Ming Xia and Chunjian Xu (2014), doi:10.1021/ie502735g
  [26] Alexandre C. Dimian, Costin S. Bildea and Anton A. Kiss (2014), doi:10.1016/B978-0-444-62700-1.00004-8
  [27] Federico Lozano Santamaría and Jorge M. Gómez (2015), doi:10.1021/ie5036594
  [28] Funmilayo Osuolale and Jie Zhang (2015), doi:10.1002/ceat.201400707
  [29] Thomas Bisgaard, Jakob Kjøbsted Huusom and Jens Abildskov (2015), doi:10.1002/aic.14970
  [30] Marcella Porru, Roberto Baratti and Jesus Alvarez (2015), doi:10.1016/j.ifacol.2015.09.121
  [31] Jian Ma, Weisong Li, Chunli Ni, Ye Li, Shanyuan Huang, Changlin Shen and Chunjian Xu (2015), doi:10.1002/jctb.4809
  [32] E. Castellanos-Sahagun and J. Alvarez (2003), doi:10.1109/ACC.2003.1238975
  [33] Ionut Muntean, Mihaela Ligia Unguresan, Andreea Savu and Mihail Abrudean (2012), doi:10.1109/AQTR.2012.6237684
  [34] E. Castellanos-Sahagun and J. Alvarez (2006), doi:10.1109/ACC.2006.1657605
  [35] Diana Ugryumova, Gerd Vandersteen, Bart Huyck, Filip Logist, Jan Van Impe and Bart De Moor (2012), doi:10.1109/I2MTC.2012.6229227
  [36] Xiaoming Jin, Gang Rong and Shuqing Wang (2000), doi:10.1109/WCICA.2000.863211
  [37] A. Kumar and P. Daoutidis (1999), doi:10.1109/ACC.1999.786281
  [38] Musch and Steiner (1994), doi:10.1109/CCA.1994.381453
  [39] Diana Ugryumova, Gerd Vandersteen, Bart Huyck, Filip Logist, Jan van Impe and Bart De Moor (2013), doi:10.1109/TIM.2012.2234577
  [40] Diana Ugryumova, Rik Pintelon and Gerd Vandersteen (2015), doi:10.1109/TIM.2015.2433612
  [41] Petar Durdevic, Simon Pedersen and Zhenyu Yang (2015), doi:10.1109/ICMA.2015.7237681
  [42] Clara Ionescu, Roxana Both, Csaba Fustos, Clement Festila, Mihai Gligan and Robin De Keyser (2015), doi:10.1109/CSCS.2015.150
  [43] Marcus V. Americano da Costa and Tito L. M. Santos (2015), doi:10.1109/IREC.2015.7110919
  [44] Diana Ugryumova, Rik Pintelon and Gerd Vandersteen (2015), doi:10.1109/TIM.2015.2454752
  [45] Pinak Pani Biswas, Subhabrata Ray and Amar Nath Samanta (2008), doi:10.3182/20080706-5-KR-1001.01723
  [46] Vishal Mahindrakar and Juergen Hahn (2016), doi:10.1016/j.conengprac.2016.04.008
  [47] Eduardo Castellanos-Sahagún, Jesús Alvarez, Andrea Frau and Roberto Baratti (2010), doi:10.3182/20100705-3-BE-2011.00010
  [48] Marcella Porru, Roberto Baratti and Jesus Alvarez (2014), doi:10.3182/20140824-6-ZA-1003.01780
  [49] Elvira Marie B. Aske, Stig Strand and Sigurd Skogestad (2005), doi:10.3182/20050703-6-CZ-1902.01647
  [50] Anna Pulis, Carlos Fernandez, Roberto Baratti and Jesus Alvarez (2006), doi:10.3182/20060402-4-BR-2902.00573
  [51] B. Pluymers and B. Vandecraen (2012), doi:10.3182/20120711-3-BE-2027.00285
  [52] Anna Pulis, Carlos Fernandez, Roberto Baratti and Jesus Alvarez (2010), doi:10.3182/20070606-3-MX-2915.00050
  [53] Adriana Reyes-Lúa, Marie Solvik and Sigurd Skogestad (2016), doi:10.1016/B978-0-444-63428-3.50107-7
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  [55] Aarón Romo-Hernandez, Denis Dochain, B. Erik Ydstie and Nicolas Hudon (2016), doi:10.1016/j.ifacol.2016.10.758
  [56] K. Kalanithi, H. Abirami, S. Malaisamy, M. Mohammed Rafiq and K. Saravanan (2016), doi:10.1109/ICEEOT.2016.7754743
  [57] S. Grüner, S. Schwarzkopf, I. Uslu, A. Kienle and E.D. Gilles (2004), doi:10.1016/S1474-6670(17)38734-7
  [58] G. Fernbolz, M. Friedrich, S. Grüne, K.-D. Mohl, A. Kienle and E.-D. Gilles (2001), doi:10.1016/S1474-6670(17)33811-9
  [59] Estiyanti Ekawati, Megarini Hersaputri and Tua Agustinus Tamba (2017), doi:10.1109/ICA.2017.8068418
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[1] ABU-EISHAH, S.I. LUYBEN, W.L. (1985). Design and control of a two-column azeotropic distillation system, Ind. Eng. Chem, Process. Des. Dev., 24, 132-140 doi:10.1021/i200028a024
[2] AL-ELG, A.H. PALAZOGLU, A. (1989). Modeling and control of a high-purity double-effect distillation column, Comput Chem. Engng., 13, 1183-1187 doi:10.1016/0098-1354(89)87021-8
[3] ALATIQI, I.M. LUYBEN, W.L. (1986). Control of a complex sidestream column/stripper distillation configuration, Ind. Eng. Chem. Process Des. Dev., 25, 762-767 doi:10.1021/i200034a028
[4] ALEJSKI, K. (1991). Computation of the reacting distillation column using a liquid mixing model on the plates, Comput. Chem. Engng., 15, 5,313-323 doi:10.1016/0098-1354(91)80005-G
[5] ALSOP, A.W. EDGAR, T.F. (1990). Nonlinear control of a high-purity distillation column by the use of partially linearized control variables, Comput. Chem. Engng., 14,665-678 doi:10.1016/0098-1354(90)87035-N
[6] ANDERSEN, H.W. KÜMMEL, M. (1991). Identifying gain directionality of multivariable processes, Proc. European Control Conference, Grenoble, 1968-1973.
[7] ANDERSEN, H.W., KÜMMEL, M., NØRGAARD, A.H. NIELSEN, K. (1988). Evaluation of controller tuning methods applied to distillation column control, Preprints 3rd Int. Symp. on Process Systems Eng..PSE´88, Sydney.
[8] ANDERSEN, H.W., KÜMMEL, M. JØRGENSEN, S.B. (1989). Dynamics and identification of a binary distillation column, Chem. Eng. Sci, 44, 2571-2581 doi:10.1016/0009-2509(89)85201-7
[9] ANDERSEN, H.W., LAROCHE, L. MORARI, M. (1991). Dynamics of homogeneous azeotropic distillation columns, Ind. Eng. Chem. Res., 30, 1846-1855 doi:10.1021/ie00056a026
[10] ANDERSEN, J.E. (1986). Multivariable control of an azeotropic distillation column, Adv. Instrum. Control, 42, 469-476.
[11] ARKUN, Y. (1988). On the use of the structured singular value for robustness analysis of distillation columns control, Comput. Chem. Engng., 12, 303-306 doi:10.1016/0098-1354(88)85042-7
[12] BALCHEN, J.G. (1990). The Stability of 2x2 multivariable control systems, Modelling Identification and Control, 11, 97-108 doi:10.4173/mic.1990.2.3
[13] BARON, G. BARRE, B. (1987). Plant scale horizontal periodic distillation - experiments and simulation, Distillation and Absorbtion 87, Brighton, UK. Published in: I. Chem. E.Symposium Services, No. 104, B51-B62.
[14] BENALLOU, A., SEBORG, D.E. MELLICHAMP, D.A. (1986). Dynamic compartmental models for separation processes, AlChE Journal, 32,1067-1078.
[15] BEQUETTE, B.W. EDGAR, T.F. (1988). A dynamic interaction index based on set point transmittance, AlChE Journal, 34,849-852.
[16] BERBER, R. KARADURMUS, E. (1989). Dynamic simulation of a distillation column separating a multicomponent mixture, Chem. Eng. Comm., 84, 113-127 doi:10.1080/00986448908940338
[17] BIRKY, G.J., McAVOY, T.J. TYRFUS, D.D. (1988). Expert system for design of distillation controls, Adv. Instrum. Control, 43,387-399.
[18] BLOCH, G, LOFFLER, C. DUBUS, J.P. (1991). Control scheme of a benzene extractive distillation plant, Preprints IFAC Symp. Adchem 91, Toulouse, France, 391-396.
[19] BOYD, D.M. (1946). Control of fractionation columns, Petr. Refiner, 25,147-151.
[20] BOZENHARDT, H.F. (1988). Modern control tricks solve distillation problems, Hydrocarbon Processing, 67, 47-50.
[21] BUCKLEY, P.S., LUYBEN, W.L. SHUNTA, F.S. (1985). Design of distillation column control systems, Instrument Society of America, Research Triangle Park, USA.
[22] CARLING, G.A. WOOD, R.K. (1987). Transient response behaviour of a depropanizer, Distillation and Absorbtion 87, Brighton. UK. Published in: I. Chem. E. Symposium Series, No. 104, B11-B24.
[23] CASTRO, R., ALVAREZ, J. ALVAREZ, J. (1990). Nonlinear disturbance decoupling control of a binary distillation column, Automatica, 26,567-572 doi:10.1016/0005-1098(90)90027-F
[24] CHAVEZ, C., SEADER, J.D. WAYBURN, T.L. (1986). Multiple steady-state solutions for interlinked separation systems, Ind. Eng. Chem. Fundam., 25, 566 doi:10.1021/i100024a017
[25] CHIANG, T-P. LUYBEN, W.L. (1985). Incentives for dual composition control in single and heat-integrated binary distillation columns, Ind. Eng. Chem. Fundam., 24, 352-359 doi:10.1021/i100019a012
[26] CHIANG, T-P. LUYBEN, W.L. (1988). Comparison of the dynamic performances of three heat-integrated distillation columns, Ind. Eng. Chem. Res., 27, 99-104 doi:10.1021/ie00073a019
[27] CHO, Y.S. JOSEPH, B. (1984). Reduced-order models for separation columns-III: Application to columns with multiple feeds and sidestreams, Comput. Chem. Engng., 8, 91-90 doi:10.1016/0098-1354(84)87015-5
[28] CHOE, Y.-S. LUYBEN, W.L. (1987). Rigorous dynamic models of distillation columns, Ind. Eng. Chem. Res., 26, 2158-2161 doi:10.1021/ie00070a038
[29] DAHLQVIST, S.A. (1981). Control of a distillation control of a distillation column using self-tuning regulators, Can. J. Chem. Eng., 50, 118-127 doi:10.1002/cjce.5450590115
[30] DAVIDSON. E.J. (1967). Control of a distillation column with pressure variation, Trans. Instn. Chem. Engrs., 45, T229.
[31] DAVIDSON, J.F. (1956). The transient behaviour of plate distillation columns, Trans. Instn. Chem. Engrs., 34, 44-52.
[32] DESPHANDE., P.B. (1985). Distillation dynamics and control, Instrument Society of America, Triangle Park, USA.
[33] DING, S.S. LUYBEN, W.L. (1990). Control of heat-integrated complex distillation configuration, Ind. Eng. Chem. Res., 29, 1240-1249 doi:10.1021/ie00103a024
[34] DOHERTY, M.F. PERKINS, J.D. (1982). On the dynamics of distillation processes IV - Uniqueness and stability of the steady-state in homogeneous continuous distillations, Chem. Eng. Sci., 37, 381-392 doi:10.1016/0009-2509(82)80090-0
[35] DOUKAS, N. LUYBEN, W.L. (1978). Control of sidestream columns separating ternary mixtures, Instrumentation Technology, 25, 43-48.
[36] DOUKAS, N. LUYBEN. W.L. (1981). Control of an energy-conserving prefractionator/sidestream column distillation system, Ind. Eng. Chem. Process Des. Dev., 20, 147-153 doi:10.1021/i200012a023
[37] DROZDOWICZ, B. MARTINEZ, E. (1988). Reduced models for separation processes in real-time simulators, Comput. Chem. Engng., 12, 547-560.
[38] EDWARDS, J.B. GUILANDOUST, M. (1986). Parametric transfer functions for packed binary distillation columns, Preprints IFAC Symp. DYCORD-86, Bournemouth, UK, 195-202.
[39] ELAAHI, A. LUYBEN, W.L. (1985). Control of an energy-conservative complex configuration of distillation columns for four-component separations, Ind. Eng. Chem. Process Des. Dev., 24, 368-376 doi:10.1021/i200029a025
[40] ESPUNA, A. PUIGIANER, L. (1988). On the solution of the retrofitting process for multiproduct batch/semicontinuous chemical plants, Preprints ChemDATA 88, Göteborg, Sweden, 296-301, Published by IVA, Stockholm.
[41] FINCO, M.V., LUYBEN, W.L. POLLECK, R.E. (1989). Control of distillation columns with low relative volatility, Ind. Eng. Chem. Res., 28, 75-83 doi:10.1021/ie00085a014
[42] FUENTES, C. LUYBEN, W.L. (1982). Comparison of energy models for distillation columns, Ind. Eng. Chem. Fundam., 21, 323-325 doi:10.1021/i100007a022
[43] GANI, R. CAMERON, I.T. (1989). Extension of dynamic models of distillation columns to steady-state simulation, Comput. Chem. Engng., 13, 271-280 doi:10.1016/0098-1354(89)85004-5
[44] GANI, R., RUIZ, C.A. CAMERON, I.T. (1986). A generalized model for distillation column-1: Model description and applications, Comput. Chem. Engng., 10, 181-198 doi:10.1016/0098-1354(86)85001-3
[45] GEORGIOU, A., GEORGAKIS, C. LUYBEN, W.L. (1988). Nonlinear dynamic matrix control for high-purity distillation columns, AIChE Journal, 34, 1287-1298 doi:10.1002/aic.690340807
[46] GILLES, E.D. RETZBACH, B. (1980). Reduced models and control of distillation columns with sharp temperature profiles, Proc. 19th IEEE Conf. on Design and Control, 865-870.
[47] GRITSIS, D., PANTELIDES, C.C. SARGENT, R.W.H. (1988). The dynamic simulation of transient systems described by index two differential-algebraic equations, Preprints 3rd Int. Symp. on Process System Engineering.PSE´88, Sydney.
[48] GROSDIDIER, P. KENNEDY, P. (1990). Case study in multi variable control - Main fraction slurry pump-around, Chem. Eng. Journal, 44, 119-127 doi:10.1016/0300-9467(90)80068-N
[49] HÄGGBLOM, K.E. (1988). Consistent control structure modeling with application to distillation control, Ph.D. Thesis, Åbo Akademi, Finland.
[50] HÄGGBLOM, K.E. (1991). Modelling of flow dynamics for control of distillation columns, Proc. American Control Conference, Boston, 785-790.
[51] HÄGGBLOM, K.E. WALLER, K.V. (1986). Relations between steady-state properties of distillation control system structures, Preprints IFAC Symp. DYCORD 89,243-248.
[52] HÄGGBLOM, K.E. WALLER, K.V. (1988). Transformations and consistency relations of distillation control structures, AlChE Journal, 34,1634-1648.
[53] HÄGGBLOM, K.E. WALLER, K.V. (1990). Control structures for disturbance rejection and decoupling of distillation, AlChE Journal, 36,1107-1113.
[54] HAJDU, H., BORUS, A. FOLDES, P. (1978). Vapor flow lag in distillation columns, Chem. Eng. Sci., 33,1-8 doi:10.1016/0009-2509(78)85060-X
[55] HALLAGER, L., JENSEN, N. JØRGENSEN, S.B. (1990). Control system configuration for a distillation column, Presented at Nordic CACE Symp., Lyngby, Denmark.
[56] HOFFMAN, D., KORCHINSKI, W., KARASIUK, C. TREIBER, S. (1988). Crude unit control with QDMC, Paper at AlChE Spring Meeting, New Orleans, LA.
[57] HOKANSON, D.A. HOCK, B.G. JOHNSON, C.R. (1989). DMC control of a complex refrigerated fractionator, Adv. Instrum. Control, 44, 541-552.
[58] HORTON, R.R., BEQUETFE, B.W. EDGAR, T.F. (1991). Improvements in dynamic compartmental modelling for distillation, Comput. Chem. Engng., 15, 197-201 doi:10.1016/0098-1354(91)85006-G
[59] HOWARD, G.M. (1970). Unsteady state behavior of multicomponent distillation columns: part I: simulation, AlChE Journal, 16, 1022-1033.
[60] HSIE, L. McAVOY, T.J. (1991). Comparison of single loop and QDMC-based control of crude oil distillation towers, J. Proc. Cont.,1, 15-21 doi:10.1016/0959-1524(91)87003-G
[61] HWANG, Y.L. (1991). Nonlinear wave theory for dynamics of binary distillation columns, AIChE Journal, 37,705-723 doi:10.1002/aic.690370509
[62] JACOBSEN, E.W. (1991). Studies on dynamics and control of distillation columns, Ph.D. Thesis, University of Trondheim, NTH, Norway.
[63] JACOBSEN, E.W. SKOGESTAD, S. (1991). Multiple Steady-States in Ideal Two Product Distillation, AlChE Journal, 30, 499-511.
[64] JACOBSEN, E.W. SKOGESTAD, S. (1991). Control of Unstable Distillation Columns, Proc. American Control Conference, Boston, 773-778.
[65] JACOBSEN, E.W. SKOGESTAD, S. (1991). Design modifications for improved control of distillation coloumns, EFChE Symposium COPE-91, Barcelona, Spain. Published in: Puigjaner and Espuna.Eds, Computer oriented Process Engineering, Elsevier, 123-128.
[66] JACOBSEN, E.W. SKOGESTAD, S. (1992). Dynamics and control of unstable distillation columns, DYCORD 92, Maryland, USA.
[67] JACOBSEN, E.W., LAROCHE, L.., SKOGESTAD, S. ANDERSEN, H.W. (1991). Robust control of homogenous azeotropic distillation columns, AlChE Journal, 37, 12,1810-1824.
[68] JACOBSEN, E.W., LUNDSTRÖM, P. SKOGESTAD, S. (1991). Modelling and identification for robust control of ill-conditioned plants - a distillation case study, Proc. American Control Conference, Boston, 242-248.
[69] JOHNSON, T.S. (1984). Computerized control scheme development of distillation columns using multiple temperature inputs systems, ISA Trans., 23,73-83.
[70] JOSEPH, B. BROSILOW, C.B. (1976). Multi-temps give better control, Hydrocarbon Processing, 127-131.
[71] JOSEPH, B., BROSILOW, C.B. TONG, M. (1978). Inferential control of processes: I- Steady state analysis, II- The structure and dynamics of inferential control systems, III- Construction of optimal and suboptimal dynamics estimators, AlChE Journal, 24, 485-509.
[72] KAPOOR, N. McAVOY, T.J. (1987). An analytical approach to approximate dynamic modelling of distillation towers, Ind. Eng. Chem. Res., 26,2473-2482 doi:10.1021/ie00072a015
[73] KAPOOR, N., McAVOY, T.J. MARLIN, T.E. (1986). Effect recycle structure on distillation tower time constants, AlChE Journal, 32, 411-424.
[74] KARLSTRÖM, A. (1991). Modelling of packed bed distillation column, Ph.D. Thesis, Chalmers Univ. of Technology, Göteborg, Sweden.
[75] KIM, H.S., LEE, K.S., YOO, K.P., LEE, W.H. PARK, H.S. (1988). Two-part modular reduced-order model for multicomponent multistage distillation columns, Journal of chemical Eng. of Japan, 22,41-47 doi:10.1252/jcej.22.41
[76] KIM, Y.H., KIM, S.Y. KIM, J.B. (1989). Adaptive control of a binary distillation column using quadratic programming, Korean J. Chem. Eng., 6, 306-312 doi:10.1007/BF02705219
[77] KIM, Y.S. McAVOY, T.J. (1981). Steady-state analysis of interaction between pressure and temperature or composition loops in a single distillation tower, Ind. Eng. Chem. Fundam., 381-388 doi:10.1021/i100004a015
[78] KING, C.J. (1971). Separation processes, McGraw-Hill, USA.
[79] KINOSHITA, M. (1986). Simple model for dynamic simulation of stage separation processes with very volatile components, AIChE Journal, 32, 872-874 doi:10.1002/aic.690320521
[80] KISTER, H.Z. (1990). Distillation operation, McGraw-Hill, New York.
[81] KOVACH, J.W. SLIDER, W.D. (1987). Heterogenous azeotropic distillation - homotopy continuation methods, Comput. Chem. Eng., 11, 593-605 doi:10.1016/0098-1354(87)87005-9
[82] KÜMMEL, M. ANDERSEN, H.W. (1987). Controller adjustment for improved nominal performance and robustness - II: Robust geometric control of a distillation column, Chem. Eng. Sci, 42, 2011-2023 doi:10.1016/0009-2509(87)80147-1
[83] KOUNG, C.W. MACGREGOR, J.F. (1991). Geometric analysis of the global stability of linear inverse-based controllers for bivariate nonlinear processes, Ind. Eng. Chem. Res., 30, 1171-1181 doi:10.1021/ie00054a016
[84] LAGAR, G., PALOSCHI, J. ROMAGNOLI J.A. (1987). Numerical studies in solving dynamic distillation problems, Comput. Chem. Eng., 11, 383-394 doi:10.1016/0098-1354(87)85019-6
[85] LANG, L. GILLES, E.D. (1989). A case-study of multivariable control for a multicomponent distillation unit on a pilot plant scale, Proc. American Control Conference, 101-106.
[86] LANG, L. GILLES, E.D. (1991). Distillation with an intermittent sidewithdrawal to control medium boiling impurities in the feed, Presented at American Control Conference, Boston.
[87] LEAR, J.B., BARTON, G.W. PERKINS, J.D. (1989). Optimising control for an industrial distillation column using a simplified model, R.A.I.R.O.APII, Argentina, 23, 221-237.
[88] LEE, M. PARK, S. (1991). Dynamic structural transformation for the analysis of distillation control structures, AIChE Journal, 37, 1725-1729 doi:10.1002/aic.690371115
[89] LEVINE., J. ROUCHON, P. (1991). Quality control of binary distillation columns via nonlinear aggregated models, Automatica, 27, 463-480 doi:10.1016/0005-1098(91)90104-A
[90] LEVY, R.S., FOSS, A.S. GRENS, E.A. (1969). Response modes of a binary distillation column, Ind Eng Chem. Fundamentals, 8, 765-776 doi:10.1021/i160032a027
[91] LEWIN, D.L. (1991). Feedforward design using the disturbance condition number, Preprints IFAC Symp. Adchem. 91, Toulouse, France, 87-92.
[92] LIN, W.J., SEADER, J.D. WAYBURN, T.L. (1987). Computing multiple solutions to systems of interlinked separation columns, AIChE, Journal, 33, 886 doi:10.1002/aic.690330603
[93] LOCKETT, J.M. (1986). Distillation tray fundamentals, Cambridge University Press.
[94] LUNDSTRÖM, P. SKOGESTAD, S. (1991). Robust and model predictive control of 5x5 distillation columns, Presented at AlChE Annual Meeting, Los Angeles.
[95] LUYBEN, W.L. (1970). Distillation decoupling, AIChE Journal, 16, 198-203 doi:10.1002/aic.690160209
[96] LUYBEN, W.L,. (1971). Control of distillation columns with sharp temperature profiles, AlChE Journal, 17, 713-718.
[97] LUYBEN, W.L. (1973). Parallel cascade control, Ind. Eng. Chem. Fundam., 12, 463-467 doi:10.1021/i160048a012
[98] LUYBEN, W.L. (1975). Steady-state energy conservation aspects of distillation column control system design, Ind. Eng. Chem. Fundam., 14, 321-325 doi:10.1021/i160056a007
[99] LUYBEN, W.L. (1979). Introduction and overview of distillation column control, Workshop Industrial Process Control, Published by AlChE, 54-58.
[100] LUYBEN, W.L. (1986). Simple method for tuning SISO controllers in multivariable systems, Ind. Eng. Chem. Process Des. Dev., 25, 654-660 doi:10.1021/i200034a010
[101] LUYBEN, W.L. (1989). The impact of process diversity on distillation column control, Preprints IFAC Symp. DYCORD + 89, Maastricht, Netherlands, 3-9.
[102] LUYBEN, W.L. (1992). Practical distillation control, Van Nostrand Reinhold, New York.
[103] MAARLEVELD, A. RIJNSDORP, J.E. (1970). Constraint control on distillation columns, Automatica, 6, 51-58 doi:10.1016/0005-1098(70)90074-9
[104] MAGNUSSEN, T., MICHELSEN, M.L. FREDENSLUND, Aa. (1979). Azeotropic distillation using UNIFAC, Inst. Chem. Eng. Symp. Ser., 54, 44.2/1-4.2/19.
[105] MANDLER, J.A., VINSON, D.R. CHATTERJEE, N. (1989). Dynamic modelling and control of cryogenic air separation plants, Preprints IFAC Symp. DYCORD + 89, Maastricht, Netherlands, 249-256.
[106] MARQUARDT, W. (1986). Nonlinear model reduction for binary distillation, Preprints IFAC Symp. DYCORD 86, Bournemouth, UK, 123-128.
[107] MARQUARDT, W. (1988). Concentration profile estimation and control in binary distillation, Preprints IFAC Workshop Model Based Process Control, Atlanta.
[108] McAVOY, T.J. (1983). Interaction analysis: Principles and applications, Instrument Society of America, Triangle Park, USA.
[109] McAVOY, T.J. WANG, Y.K. (1986). Survey of recent distillation control results, ISA Trans., 25, 1,5-21.
[110] McAVOY, T.J. WEISCHEDEL, K. (1981). A dynamic comparison of material balance versus conventional control of distillation columns, Proc. VIII IFAC World Congress, Kyoto, XXII, 109-114.
[111] McCUNE, L.C. GALLIER, P.W. (1973). Digital Simulation: A tool for the analysis and design of distillation controls, ISA Trans., 12, 193-207.
[112] MCDONALD, K.A. McAVOY, T.J. (1987). Application of dynamic matrix control to moderate- and high-purity distillation towers, Ind. Chem. Chem. Res., 26,1011-1018 doi:10.1021/ie00065a027
[113] MCDONALD, K.A., PALAZOGLU, A. BEQUETTE, B.W. (1988). Impact of model uncertainty descriptions for high-purity distillation control, AIChE Journal, 34, 1996-2004.
[114] MCGREAVY, C. TAN, G.H. (1986). Effect of process and mechanical design on the dynamics of distillation columns, Preprints IFAC Symp. DYCORD-86, Bournemouth, UK, 181-188.
[115] MEJDELL, T. SKOGESTAD, S. (1991). Estimation of distillation composition from multiple temperature measurements using PLS regression, Ind. Eng. Chem. Res., 30, 12, 2543-2355 doi:10.1021/ie00060a007
[116] MEJDELL, T. SKOGESTAD, S. (1991). Composition estimator in a pilot plant distillation column using multiple temperatures, Ind Eng. Chem. Res., 30, 12,2555-2564 doi:10.1021/ie00060a008
[117] MIZSEY, P., HAJDU, H. FOLDES, P. (1987). How construction affects column control, Hydrocarbon Processing, 66, 53-56.
[118] MOORE, C., HACKNEY, J. CANTER, D. (1987). Selecting sensor location and type for multivariable processes, In: Prett, D.M. and Morari, M., Shell Process Control Workshop, Butterworth.
[119] MORRISON, T.A. LAFLAMME, D. (1990). Advanced controls improve performance of two-shell, dualpressure column, Oil and Gas Journal, 88,60-63.
[120] MUHRER, C.A., COLLURE, M.A. LUYBEN, W.L. (1990). Control of vapor recompression distillation columns, Ind. Eng. Chem. Res., 29, 59-71 doi:10.1021/ie00097a010
[121] MUSKE, K., YOUNG, J., GROSDIDIER, P. TANI, S. (1991). Crude unit product quality control, Comput. Chem. Engng., 15, 629-638 doi:10.1016/0098-1354(91)87024-4
[122] NAKA, Y. O´SHIMA, E. (1986). Control of a distillation column with a heat pump, Preprints IFAC Symp. DYCORD -86, Bournemouth, UK, 261-266.
[123] NIELSEN, C.S., ANDERSEN, H.W., BRABRAND, H JØRGENSEN, S.B. (1988). Adaptive dual composition control of a binary distillation column with heat pump, Preprints IFAC Symp. on Adaptive Control of Chem. Processes.Adchem, Lyngby, Denmark, 220-225.
[124] NIELSEN, C.S., ANDERSEN, H.W., BRABRAND, H., TOFTEGÅRD, B., CLEMENT, K. JØRGENSEN, S.B. (1988). Identification and adaptive control of a binary distillation column with heat pump, Presented at ChemDATA 88, Göteborg.
[125] NISENFELD, A.E. SEEMAN, K.C. (1981). Distillation columns, Instrument Society of America.ISA, Triangle Park, USA.
[126] PAPASTATHOPOULOU, H.S. LUYBEN, W.L. (1991). Control of a binary sidestream distillation column, Ind. Eng. Chem. Res., 30, 705-713 doi:10.1021/ie00052a013
[127] PATWARDHAN, A. EDGAR, T. (1991). Nonlinear predictive control of packed distillation column, Proc. American Control Conference, Boston, 767-772.
[128] PERRY, R.H. CHILTON, C.H. (1973). Chemical engineers´ handbook, McGraw-Hill, New York.
[129] PINTO, J.C. BISCAIA, E.C. (1988). Order reduction strategies for models of staged separation systems, Comput. Chem. Engng., 12, 821 doi:10.1016/0098-1354(88)80020-6
[130] PRETT, D.M. MORARI, M. (1987). Shell process control workshop, Butterworth Publisher, MA, USA.
[131] PROKOPAKIS, G.J. SEIDER, W.D. (1983). Feasible specifications in azeotropic distillation, AIChE Journal, 29, 1, 49-60 doi:10.1002/aic.690290107
[132] RADEMAKER, O.J., RIJNSDORP, J.E. MAARLEVELD, A. (1975). Dynamics and control of continuous distillation columns, Elsevier. Amsterdam.
[133] RASMUSSEN, K. H., NIELSEN, C. S. JØRGENSEN, S. B. (1990). Identification of distillation process dynamics comparing process knowledge and black box based approaches, Proc. American Control Conference, San Diego, 3116-3121.
[134] RETZBACH, B. (1986). Control of an extractive distillation plant, Preprints IFAC Symp. DYCORD -86, Bournemouth, UK, 225-230.
[135] RHIEL, F.F. KRAHL, F. (1988). A model-based control system for a distillation column, Chem. Eng. Technol., 11, 188-194 doi:10.1002/ceat.270110125
[136] ROFFEL, B. RUNSDORP, J.E. (1982). Process dynamics, control and protection, Ann Arbor Science, Ann Arbor, USA.
[137] ROSENBROCK, H.H. (1962). Distinctive problems of process control, Chem. Eng. Progress. 58, 43-50.
[138] ROSENBROCK, H.H. (1962). The control of distillation columns, Trans. Instn. Chem. Engrs., 40, 35-53.
[139] ROSENBROCK, H.H. (1962). A Lyapunov function with applications to some nonlinear physical systems, Automatica, 1, 31-53 doi:10.1016/0005-1098(63)90005-0
[140] ROSENBROCK, H.H. (1962). The transient behaviour of distillation columns and heat exchangers: An historical and critical review, Trans. Instn, Chem. Engrs., 40, 376-384.
[141] ROVAGLIO, M. DOHERTY, M. (1990). Dynamics of heterogeneous azeotropic distillation columns, AlChE Journal, 36, 39-52.
[142] ROVAGLIO, M., RANZI, E., BIARDI, G. FARAVELLI, T. (1990). Rigorous dynamics and control of continuous distillation systems - Simulation and experimental result, Comput. Chem. Engng., 14, 871-887 doi:10.1016/0098-1354(90)87042-N
[143] ROVAGLIO, M., RANZI, E, MARDI, G., FONTANA, M. DOMENICHINI, R. (1990). Rigorous dynamics and feedforward control design for distillation processes, AlChE Journal, 36, 576-586.
[144] ROVAGLIO, M., FARAVELI,I, T. DOHERTY, M. F. (1991). Operability and control of azeotropic heterogeneous distillation sequences, Proc. Systems Engineering.PSE´91, Montebello, Canada, II.17.1-17.15.
[145] RUIZ, C.A. GANI, R. (1986). Simulation and design of distillation columns part I: Hydraulic model and dynamic behavior, Lat. Am. J. Chem. Eng. Appl. Chem., 277-205.
[146] RYSKAMP, C.J. (1980). New strategy improves dual composition column control, Hydrocarbon Process, 60, 51-59.
[147] RYSKAMP, C.J. (1982). Explicit versus implicit decoupling in distillation control, In: Seborg and Edgar.Eds, Chemical Process Control 2, Published by AIChE, New York, 361-376.
[148] SANDELIN, P.M., HÄGGBLOM, K.E. WALLER, K.V. (1991). Disturbance rejection properties of control structures at one-point control of a two-product distillation column, Ind. Eng. Chem. Res., 30, 1187-1193 doi:10.1021/ie00054a018
[149] SANDELIN, P.M., TOIVONEN, H.T., OSTERAS, M. WALLER, K.V. (1991). Robust multiobjective linear quadratic control of distillation using low-order controllers, Chem. Eng. Sci., 46,2815-2827 doi:10.1016/0009-2509(91)85151-M
[150] SCALI, C. BRAMBILLA, A. (1987). Controllers design for a multi-product distillation unit in the presence of uncertainty, Distillation and Absorbtion 87, Brighton, UK. Published in: I. Chen. E. Symposium Series, No. 104, B63-B74.
[151] SEIDER, W.D., BENGEL, D.D., PROVOST, A.M. WIDAGDO, S. (1990). Nonlinear analysis in process design: Why overdesign to avoid complex nonlinearities, Ind. Eng. Chem. Res., 29, 805-818 doi:10.1021/ie00101a016
[152] SEIDER, W.D., BRENGEL, D.D. WIDAGDO, S. (1991). Nonlinear analysis in process design, AlChE Journal, 37, 1-38.
[153] SHAKOURI, A. (1986). Multivariate control of industrial fractionators, Application of multivariable control in an integrated control system. Preprints IFAC Symp. DYCORD -86, Bournemouth, UK, 49-54.
[154] SHIMIZU, K. MAH, R.S.H. (1983). Pole assignment in binary SRV distillation, Comput. Chem. Engng., 7, 123-127 doi:10.1016/0098-1354(83)85013-3
[155] SHIMIZU, K. MATSUBARA, M. (1984). Decoupling and disturbance rejection control of a binary distillation column with pressure variation, J. Chem. Eng. Japan, 17, 262-269 doi:10.1252/jcej.17.262
[156] SHIMIZU, K., HOLT, B.R., MORARI, M. MAH, R.S.H. (1985). Assessment of control structures for binary distillation columns with secondary reflux and vaporization, Ind. Eng. Chem. Process Des. Dev., 24, 852-858 doi:10.1021/i200030a055
[157] SHINSKEY, F.G. (1967). Process-control systems, 1st Edition, McGraw-Hill, New York.
[158] SHINSKEY, F.G. (1977). Distillation control, 1st Edition, McGraw-Hill, New York.
[159] SHINSKEY, F.G. (1984). Distillation control, 2nd Edition, McGraw-Hill, New York.
[160] SKJELLUM, A. (1990). Concurrent dynamic simulation, Ph.D. Thesis, California Institute of Technology.
[161] SKOGESTAD, S. (1988). Disturbance Rejection in Distillation Columns, Preprints ChemDATA 88, 19th European Conf. on the Use of Computers in Chem. Eng., Göteborg, 365-371, Published by IVA, Stockholm, Sweden.
[162] SKOGESTAD, S. (1989). Modelling and control of distillation columns as 5x5 systems, Dechema Monographs, 116.Ed.: R. Eckermann, 403-411.
[163] SKOGESTAD, S. (1991). Consistency of steady-state models using insight about extensive variables, Ind. Eng. Chem. Res., 30, 4,499-511 doi:10.1021/ie00052a009
[164] SKOGESTAD, S. (1991). Modelling and dynamic simulation for process control, Lecture notes for seminar on Modelling and Optimization of Chemical Processes, NTH, Trondheim, Norway.
[165] SKOGESTAD, S. HOVD, M. (1990). Use of frequency-dependent RCA for control structure selection, Proc. American Control Conference, San Diego, 2133-2139.
[166] SKOGESTAD, S. LUNDSTRÖM, P. (1990). Mu-optimal LV-control of Distillation Columns, Comput Chem. Engng., 14, 4/5,401-413 doi:10.1016/0098-1354(90)87016-I
[167] SKOGESTAD, S. MORARI, M. (1987). The dominant time constant for distillation columns, Comput. Chem. Engng., 11, 607-617 doi:10.1016/0098-1354(87)87006-0
[168] SKOGESTAD, S. MORARI, M. (1987). A systematic approach to distillation column control, Distillation and Absorbtion 87, Brighton, UK. Published in: L Chem. E. Symposium Series, 104, A71-A86.
[169] SKOGESTAD, S. MORARI, M. (1987). Implications of large RCA-elements on control performance, Ind. Eng. Chem. Res., 26, 2323-2330 doi:10.1021/ie00071a025
[170] SKOGESTAD, S. MORARI, M. (1987). Control configuration selection for distillation columns, AlChE Journal, 33,10,1620-1635.
[171] SKOGESTAD, S. MORARI, M. (1988). Understanding the dynamic behavior of distillation columns, Ind. Eng. Chem. Res., 27, 10,1848-1862 doi:10.1021/ie00082a018
[172] SKOGESTAD, S. MORARI, M. (1988). LV-Control of a high-purity distillation column, Chem. Eng. Sci., 43, 33-48 doi:10.1016/0009-2509(88)87124-0
[173] SKOGESTAD, S., MORARI, M. DOYLE, J.C. (1988). Robust control of ill-conditioned plants: High-purity distillation, IEEE Trans. Autom. Control, 33, 1092-1105 doi:10.1109/9.14431
[174] SKOGESTAD, S., JACOBSEN, E.W. LUNDSTRÖM, P. (1990). Modelling requirements for robust control of distillation columns, Preprints 11th IFAC Conference, Tallin, Estonia, 11, 213-219.
[175] SKOGESTAD, S., JACOBSEN, E.W. MORARI, M. (1990). Inadequacy of steady state analysis for feedback control: Distillate-bottom control of distillation columns, Ind. Eng. Chem. Res., 29, 12, 2339-2346 doi:10.1021/ie00108a006
[176] SKOGESTAD, S., LUNDSTRÖM, P. JACOBSEN, E. W. (1990). Selecting the best distillation control structure, AlChE Journal, 36, 5, 753-764.
[177] SOURANDER, M.L. GROS, S. (1986). Controlling and optimizing integrated fractionation processes in petroleum refinery, Preprints IFAC Symp. DYCORD -86, Bournemouth, UK, 61-66.
[178] STATHAKI, A., MELLICHAMP, D. A. SEBORG. D. E. (1985). Dynamic simulation of a multicomponent distillation column with asymmetric dynamics, Can. J. Chem. Eng., 63, 510-518 doi:10.1002/cjce.5450630321
[179] STEWART, W. E., LEVIEN, K. L. MORARI, M. (1983). Simulation of fractionation by orthogonal collocation, Chem. Eng. Sci., 40, 409-421 doi:10.1016/0009-2509(85)85103-4
[180] TAKAMATSU, T., HASHIMOTO, I. HASHIMOTO, Y. (1987). Selection of manipulated variables to minimize interaction in multivariate control of a distillation column, Int. Chem. Eng., 27, 669-667.
[181] TOFTEGÅRD, B. JØRGENSEN, S. B. (1987). Operational principles for periodic cycled separation, Distillation and Absorbtion 87, Brighton, UK. Published in: I. Chem. E. Symposium Series, 104, A.473-A.482.
[182] TOFTEGÅRD, B. JØRGENSEN, S.B. (1988). Stationary profiles for periodic cycled separation columns: linear case, Ind. Eng. Chem. Res., 481-485 doi:10.1021/ie00075a018
[183] TOLLIVER, T.L. McCUNE., L.C. (1980). Finding the optimum temperature control trays for distillation columns, In Tech, 75-80.
[184] TOLLIVER, T.L. WAGGONER, R.C. (1980). Distillation column control: A review and perspective from the CPI ISA Adv Instrum, 35, 83-106.
[185] TRAN, C. CUTLER, C. (1989). Dynamic matrix control on benzene and toluene towers, ISA Trans., 44, 533-539.
[186] WAHL, E.F. HARRIOT, P. (1970). Understanding and prediction of the dynamic behavior of distillation columns, Ind. Eng. Chem. Process Des. Dev., 9, 396-407 doi:10.1021/i260035a007
[187] WALLER, K.V. (1982). University research on dual composition control of distillation: A review, In Seborg, D.E. and Edgar, T.F., Chemical Process Control 2, Sea Island, Published Engineering Foundation/AlChE, 395-412.
[188] WALLER, K.V. (1986). Distillation control system structures, Preprints IFAC Symp. DYCORD 86, Bournemouth, UK, 1-10.
[189] WALLER, K. V. (1988). Presentation at AlChE Annual Meeting, Washington, DC.
[190] WALLER, K. V. (1992). Experimental comparisons of control structures, In: W.L. Luyben.Ed., Practical distillation control, Van Nustrand Reinhold, New York.
[191] WALLER, K. V. FINNERMAN, D. H. (1987). On using sums and differences to control distillation, Chem. Eng. Comm., 56, 253-268 doi:10.1080/00986448708911949
[192] WALLER, K. V., FINNERMAN, D. H., SANDELIN, P. M., HÄGGBLOM, K. E. GUSTAFSSON, S. E. (1988). An experimental comparison of four control structures for two-point control of distillation, Ind. Eng. Chem. Res., 27, 624-630.
[193] WALLER, K. V., HÄGGBLOM, K. E., SANDELIN, P.M. FINNERMAN, D.H. (1988). Disturbance sensitivity of distillation control structures, AIChE Journal, 34, 853-858 doi:10.1002/aic.690340516
[194] WEIGAND, W.A., JHAWAR, A.K. WILLIAMS, T.J. (1972). Calculation method for the response time to step inputs for approximate dynamic models of distillation columns, AlChE Journal, 18, 1243.
[195] WEISCHEDEL, K. McAVOY, T.J. (1980). Feasibility of decoupling in conventionally controlled distillation columns, Ind. Eng. Chem. Fundam., 19, 379-384 doi:10.1021/i160076a010
[196] WHITEHEAD, D.B. PARNIS, M. (1987). Computer control improves ethylene plant operation, Hydrocarbon Processing, 105-108.
[197] WIDAGDO, S., SEIDER, W. D. SEBASTIAN, D. H. (1989). Bifurcation analysis in heterogeneous azeotropic distillation, AlChE Journal. 35. 1457-1464.
[198] WILDER, C.T. SHAH, P.N. (1989). The evolution of a distillation tower advanced control strategy, Adv. Instrum. Control, 44, 103-106.
[199] WOINET, R., THOMAS, G. BORDET, J. (1991). Adaptive control based on pole placement: An experimental test on a binary distillation column, Chem. Eng. Sci., 46, 949-957 doi:10.1016/0009-2509(91)85088-F
[200] WONG, K.T. LUUS, R. (1980). Model reduction of high-order multistage systems by the method of orthogonal collocation, Can. Jour. Chem. Eng., 58, 382-388 doi:10.1002/cjce.5450580315
[201] WONG, D.S.H., JANG, S.S. CHANG, C.F. (1991). Simulation of dynamics and phase pattern changes for an azeotropic distillation column, Comput. Chem. Engng., 15, 325-355 doi:10.1016/0098-1354(91)80006-H
[202] WOOD, R.K. BERRY, M.W. (1973). Terminal composition control of a binary distillation column, Chem. Eng. Sci., 28, 1707-1717 doi:10.1016/0009-2509(73)80025-9
[203] WOZNY, G., FIEG, G., JEROMIN, L. GULICH, H. (1989). Design and operation of a state observer for the temperature front of a rectification column, Chemical Engineering Technology, 12, 339-344 doi:10.1002/ceat.270120147
[204] YANG, D.R., WALLER, K.V., SEBORG, D. E. MELLICHAMP, D.A. (1990). Dynamic structural transformations for distillation control configurations, AlChE Journal, 36, 1391.
[205] YANG, D.R., SEBORG, D.E. MELLICHAMP, D.A. (1991). Combined balance control structure for distillation columns, Ind. Eng. Chem. Res., 30, 8, 215-216.
[206] YU, C.-C. LUYBEN, W.L. (1987). Control of multicomponent distillation columns using rigorous composition estimators, I. Chem. E. Symp. Ser., 104, A.29-A.69.

  title={{Dynamics and Control of Distillation Columns - A Critical Survey}},
  author={Skogestad, Sigurd},
  journal={Modeling, Identification and Control},
  publisher={Norwegian Society of Automatic Control}


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