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Nonlinear dynamics of reactive distillation processes for the production of fuel ethers

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Kienle,  A.
Process Synthesis and Process Dynamics, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;
Otto-von-Guericke-Universität Magdeburg, External Organizations;

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Gilles,  E. D.
Integrated Navigation Systems, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;
Systems Biology, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;

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Sundmacher,  Kai
Process Systems Engineering, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;
Otto-von-Guericke-Universität Magdeburg, External Organizations;

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Citation

Mohl, K. D., Kienle, A., Gilles, E. D., Rapmund, P., Sundmacher, K., & Hoffmann, U. (1997). Nonlinear dynamics of reactive distillation processes for the production of fuel ethers. Computers and Chemical Engineering, 21(Suppl.), S989-S994.


Cite as: https://hdl.handle.net/11858/00-001M-0000-0013-A37C-A
Abstract
A rigorous numerical bifurcation and stability analysis of reactive distillation processes for the production of fuel ethers MTBE and TAME is presented. The bifurcation behaviour is studied in terms of operating conditions such as reflux ratio R and bottom flow rate B or the heating rate Q of the reboiler, respectively. Further domains of attraction and the transient behaviour towards different stable steady states are studied exemplarily using dynamic simulation. From the size and location of the multiplicity regions in the parameter space of the input variables some conclusions are drawn for process operation.