Skip to main content
Log in

Thermal runaway prevention in catalytic packed bed reactor by solid temperature measurement and Control

  • Published:
Korean Journal of Chemical Engineering Aims and scope Submit manuscript

Abstract

Magnetic crystallite thermometry has been used to measure the average nickel crystallite temperature in packed bed reactors during ethane hydrogenolysis, an exothermic reaction. The technique is based on the temperature dependence of the magnetic moment of dispersed nickel catalysts. Measurement of the average catalyst temperature is very useful for reactor control because of its shorter time constant compared with exit fluid temperature. Bed temperature control based on the exit fluid temperature, which has often been used as a control variable, is too slow to protect thermal runaway of the bed. The advantage of short time constant by measuring the average catalyst temperature has been incorporated with enhanced feedback control system to control the bed temperature and prevent the thermal runaway of the catalyst bed. An enhanced feedback control structure with supervisory action performed better than the classical proportional-integral control in runaway prevention when the two control schemes were compared with each other on the basis of the trippoint (incipient thermal runaway).

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. Giger, G. K., Mutharasan, R. and Coughanowr, D. R.:Ind. Eng. Chem. Fundam.,19, 389(1980).

    Article  CAS  Google Scholar 

  2. Froment, C. F. and Bischoff, K. B.: “Chemical Reactor Analysis and Design” John Wiley and Sons. NY (1979).

  3. Satterfield, C. N.: “Heterogeneous Catalysis in Practice” McGraw-Hill, NY (1980).

  4. Morbidelli, M. and Varma, A.:AIChE J. 32(2), 297 (1986).

    Article  CAS  Google Scholar 

  5. Cho, C. K.: Ph. D. Dissertation, Arizona State University, Tempe, AZ (1990).

  6. Barkelew, C. H.:Chem. Eng. Progr. Ser:,55(25), 37 (1959).

    Google Scholar 

  7. McGreavy, C. and Adderley, C. I.:Chem. Eng. Sci.,28, 577(1973).

    Article  CAS  Google Scholar 

  8. Kardos, P.W. and Stevens, W. F.:AIChE J.,17(5), 1090 (1971).

    Article  CAS  Google Scholar 

  9. Silva, J. M., Wallman, P. H. and Foss, A. S.:Ind. Eng. Chem. Fundam.,18(4), 383(1979).

    Article  CAS  Google Scholar 

  10. Cale, T. S.:J. Catal. 90(1), 40(1984).

    Article  CAS  Google Scholar 

  11. Ludlow, D.K.:Ph. D. Thesis, Arizona State University, Tempe, AZ (1986).

  12. Emig, G., Hofmann, H. and Fiand, U.:Chem. Eng. Sci.,35, 249(1980).

    Article  CAS  Google Scholar 

  13. Gigax,R.:Chem. Eng. Sci.,43(8), 1759(1988).

    Article  Google Scholar 

  14. Bilous, O. and Amundson, N. R.:AIChE J.,2, 117 (1956).

    Article  CAS  Google Scholar 

  15. Cho, C. K., Mersnn, J. A. and Cale, T. S.:Rev. Sci. Instrum.. 61(8), 2232(1990).

    Article  CAS  Google Scholar 

  16. Seborg. D. E.. Edgar. T. F. and Mellichamp. D. A.: “Process Dynamics and Control” John Wiley and Sons, NY(1989).

  17. Park, J. H. and Cale, T. S.: In Preparation (1992).

Download references

Author information

Authors and Affiliations

Authors

Rights and permissions

Reprints and permissions

About this article

Cite this article

Cho, CK., Chang, K.S. & Cale, T.S. Thermal runaway prevention in catalytic packed bed reactor by solid temperature measurement and Control. Korean J. Chem. Eng. 10, 195–202 (1993). https://doi.org/10.1007/BF02705267

Download citation

  • Received:

  • Accepted:

  • Issue Date:

  • DOI: https://doi.org/10.1007/BF02705267

Keywords

Navigation