Low-order dynamic models for ideal multicomponent distillation processes using nonlinear wave propagation theory

A new approach to the development of low-order dynamic models for multicomponent distillation processes is presented. This approach makes direct use of well-known spatio-temporal pattern formation phenomena also termed as nonlinear wave propagation. It takes into account the typical features of multicomponent systems, i.e. coexistence of different constant pattern waves within a single section of a distillation column and the resulting wave interactions. In a first step, constant molar holdups and flow rates, constant pressure and constant relative volatilities are assumed. Under these conditions a rigorous analytical treatment is possible and a comparably simple but sound and robust method for nonlinear model reduction is developed. The approach applies to packed as well as staged columns provided the number of column stages is sufficiently large. Application is demonstrated for two different distillation processes with a three and a five component mixture, respectively. It is shown that the dynamic behaviour of the low-order model is in good agreement with corresponding reference model for a large set of operating conditions. Finally, extensions of the present approach to processes with variable molar flow rates as well as variable volatilities are discussed.

[1]  Ross Taylor,et al.  Multicomponent mass transfer , 1993 .

[2]  Ernst Dieter Gilles,et al.  Reduced models and control of distillation columns with sharp temperature profiles , 1980 .

[3]  B. Bequette Nonlinear control of chemical processes: a review , 1991 .

[4]  Shock layer analysis in multicomponent chromatography and countercurrent adsorption , 1994 .

[5]  Wolfgang Marquardt,et al.  Development of a Linear Distillation Model from Design Data for Process Control , 1993 .

[6]  Y. Hwang,et al.  Experimental study of wave propagation dynamics of binary distillation columns , 1996 .

[7]  Y. Hwang,et al.  Dynamics of continuous countercurrent mass-transfer processes—IV. Multicomponent waves and asymmetric dynamics , 1990 .

[8]  F. Helferich,et al.  Multicomponent Chromatography—Theory of Interference , 1977 .

[9]  E. D. Gilles,et al.  DIVA - Eine Umgebung zur Simulation, Analyse und Optimierung verfahrenstechnischer Prozesse , 1997 .

[10]  Y. Hwang,et al.  Nonlinear wave theory for dynamics of binary distillation columns , 1991 .

[11]  Wolfgang Marquardt Concentration profile estimation and control in binary distillation , 1988 .

[12]  B. Retzbach Control of an Extractive Distillation Plant , 1986 .

[13]  Yng-Long Hwang,et al.  Dynamics of continuous countercurrent mass-transfer processes—III. Multicomponent systems , 1989 .

[14]  Wolfgang Marquardt,et al.  DIVA - A powerful tool for dynamic process simulation , 1988 .

[15]  Rutherford Aris,et al.  Theory and application of hyperbolic systems of quasilinear equations , 1989 .

[16]  Wolfgang Marquardt NONLINEAR MODEL REDUCTION FOR BINARY DISTILLATION , 1986 .

[17]  F. Allgower,et al.  Nonlinear H/sub /spl infin//-control of a high purity distillation column , 2002 .

[18]  Walter Murray Wonham,et al.  Towards an abstract internal model principle , 1976, 1976 IEEE Conference on Decision and Control including the 15th Symposium on Adaptive Processes.

[19]  Wolfgang Marquardt,et al.  DIVA—an open architecture for dynamic simulation , 1990 .

[20]  Ernst Dieter Gilles,et al.  Dynamische Prozeß- und Anlagensimulation , 1994 .