Skip to main content
Log in

Integrated design of power- and resource-saving chemical processes and process control systems: Strategy, methods, and application

  • Published:
Theoretical Foundations of Chemical Engineering Aims and scope Submit manuscript

Abstract

A strategy for the integrated design of power-and resource-saving chemical processes and the systems controlling their operating conditions with uncertain input data on physicochemical and process parameters is formulated. A multistep iterative procedure for solving integrated design problems is developed. The procedure includes the generation of alternative chemical processes meeting the “rigid” and/or “soft” flexibility constraints and the choice of operating (control) actions, the synthesis of alternative systems for the automatic control of the operating conditions of the chemical process and the choice of the best control system, the pairwise comparison of feasible automated integrated systems consisting of the chemical engineering process and its control system and the choice of the best integrated system using the criterion based on the power and resource savings and control quality by solving one-and/or two-stage stochastic optimization problems with rigid and/or soft constraints. An example integrated design of the flexible continuous synthesis of azo pigments with an automatic-control system for stabilizing the optimal static conditions is discussed.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

References

  1. Kafarov, V.V., Metody Kibernetiki v Khimii i Khimicheskoi Tekhnologii (Methods of Cybernetics in Chemistry and Chemical Engineering), Moscow: Khimiya, 1971.

    Google Scholar 

  2. Devyatov, B.N., Teoriya perekhodnykh protsessov v tekhnologicheskikh apparatakh s tochki zreniya zadach upravleniya (Theory of Transient Operations in Process Plants from the Viewpoint of Process-Control Problems), Novosibirsk: Sib. Otd. Akad. Nauk SSSR, 1964.

    Google Scholar 

  3. Anisimov, I.V., Bodrov, V.I., and Pokrovskii, V.B., Matematicheskoe modelirovanie i optimizatsiya rektifikatsionnykh ustanovok (Mathematical Simulation and Optimization of Distillation Columns), Moscow: Khimiya, 1975.

    Google Scholar 

  4. Bodrov, V.I., Dvoretskii, S.I., and Dvoretskii, D.S. Optimal Design of Power-and Resource-Saving Processes and Equipment in Chemical Engineering, Teor. Osn. Khim. Tekhnol., 1997, vol. 31,no. 5, p. 542 [Theor. Found. Chem. Eng. (Engl. Transl.), vol. 31, no. 5, p. 494].

    Google Scholar 

  5. Volin, Yu.M. and Ostrovskii, G.M., Optimal Design of Chemical Engineering Processes with Partially Uncertain Input Information, Avtom. Telemekh., 1995, no. 2, p. 85.

  6. Haleman, K.R. and Grossmann, I.E., Optimal Process Design Under Uncertainty, AIChE J., 1983, no. 3, p. 425.

  7. Ostrovskii, G.M., Volin, Yu.M., Barit, E.I., and Senyavin, M.M., Optimal Design of Chemical Engineering Processes under Uncertainty, Teor. Osn. Khim. Tekhnol., 1993, vol. 27,no. 2, p. 183.

    CAS  Google Scholar 

  8. Grossmann, I.E. and Morari, M., Operability, Resilience and Flexibility — Process Design Objectives for Changing World, Proc. 2nd Int. Conf. on Foundations of Computer Aided Process Design, Snowmass Village, Colorado, 1983.

    Google Scholar 

  9. Luyben, M.L. and Floudas, C.A., Analyzing the Interaction of Design and Control: 1. A Multiobjective Framework and Application to Binary Distillation Synthesis, Comput. Chem. Eng., 1994, vol. 18, p. 933.

    Article  CAS  Google Scholar 

  10. Ostrovsky, G.M., Volin, Y.M., Dvoretsky, D.S., and Dvoretsky, S.I., Integrated Design of Energy-Saving Chemical Process Systems: Strategy, Methods and Implementation, 16th European Symposium on Computer Aided Process Engineering (ESCAPE’16), Garmish-Partenkirchen, 2006, p. 521.

  11. Mamontov, I.N., Development of Algorithms of Optimal Design for Automated Chemical Engineering Plants, Cand. Sci. (Techn.) Dissertation, Tambov: TGTU., 1999.

    Google Scholar 

  12. Ostrovskii, G.M., Volin, Yu.M., and Ziyatdinov, N.N., Optimizatsiya v khimicheskoi tekhnologii (Optimization in Chemical Engineering), Kazan: FEN Akademii Nauk RT, 2005.

    Google Scholar 

  13. Devyatov, B.N., Teoriya perekhodnykh protsessov v tekhnologicheskikh apparatakh s tochki zreniya zadach upravleniya (Theory of Transient Processes in Process Plants from the Viewpoint of Process-Control Problems), Novosibirsk: Sib. Otd. Akad. Nauk SSSR, 1964.

    Google Scholar 

  14. Ostrovskii, G.M., Volin, Yu.M., and Golovashkin, D.V., Flexibility and Optimization of Chemical Technological Processes: New Approaches, Teor. Osn. Khim. Tekhnol., 1997, vol. 31, no. 2, p. 202 [Theor. Found. Chem. Eng. (Engl. Transl.), vol. 31, no. 2, p. 175].

    Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to D. S. Dvoretskii.

Additional information

Original Russian Text © D.S. Dvoretskii, S.I. Dvoretskii, G.M. Ostrovskii, 2008, published in Teoreticheskie Osnovy Khimicheskoi Tekhnologii, 2008, Vol. 42, No. 1, pp. 29–39.

Rights and permissions

Reprints and permissions

About this article

Cite this article

Dvoretskii, D.S., Dvoretskii, S.I. & Ostrovskii, G.M. Integrated design of power- and resource-saving chemical processes and process control systems: Strategy, methods, and application. Theor Found Chem Eng 42, 26–36 (2008). https://doi.org/10.1134/S0040579508010041

Download citation

  • Received:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1134/S0040579508010041

Keywords

Navigation