Simulating Trambouze reaction for a series reactor

Authors

  • Amizon Azizan Faculty of Chemical Engineering, Universiti Teknologi MARA, Shah Alam, Selangor, Malaysia
    • Nornizar Anuar Faculty of Chemical Engineering, Universiti Teknologi MARA, Shah Alam, Selangor, Malaysia

      DOI:

      https://doi.org/10.24191/mjcet.v3i1.10930

      Keywords:

      Continuous stirred tank reactor, Plug flow reactor, Selectivity, Conversion, Desired product

      Abstract

      Simulating the existing data on Trambouze reaction is compiled in this article. The objective of the work is to present the change of volumetric flow rate and the inlet concentration of key reactant A in a series continuous stirred tank reactor-plug flow reactor (CSTR-PFR) configurations. The volumetric flow rate does not affect selectivity and conversion for a constant volumetric flow rate operating condition, entering CSTR and PFR, at a specific concentration of reactant. The CSTR-PFR series reactor configuration is proposed for the aim of maximizing the selectivity of the desired product B in comparison to the undesired products X and Y. CSTR as the first reactor is capable to achieve the maximum conversion at the highest selectivity of A. PFR is then proposed after CSTR in a configuration of CSTR-PFR, to allow higher conversion value to be achieved for the resulted outlet stream conditions coming out of the first reactor, CSTR. Both reactors commonly encounter a decrease in the initial concentration of A and an increase to the formation of other products. The CSTR entering volumetric flow rate influence the volume sizes needed in achieving the maximum selectivity and conversion.

      References

      A. C. Kokossis & C. A. Floudas (1990). Optimization of complex reactor networks—I. Isothermal

      operation. Chemical Engineering Science, 45(3), 595–614.

      A. Varma & A. L. DeVera (1979). Dynamics of selectivity reactions in isothermal CSTRs. Chemical Engineering Science, 34(12), 1377–1386.

      H. S. Fogler, (2014). Elements of Chemical Reaction Engineering. Chapter 6. England: Pearson

      Education Limited.

      J. D. Paynter & D. E. Haskins (1970). Determination of optimal reactor type. Chemical Engineering

      Science, 25(9), 1415–1422.

      J. K. Bandyopadhyay, V. Ravikumar & B. D. Kulkarni (1993). Altering the conversion/selectivity

      behaviour for a CSTR exhibiting chaotic dynamics. Industrial & engineering chemistry

      research, 32(12), 2953–2959.

      L. E. Achenie & L. T. Biegler (1986). Algorithmic synthesis of chemical reactor networks using

      mathematical programming. Industrial & engineering chemistry fundamentals, 25(4), 621–

      L.K. da Silva, M. A. D. S. S. Ravagnani, G. P. Menoci & M. M. A. Samed (2008). Reactor network

      synthesis for isothermal conditions. Acta Scientiarum. Technology, 30(2), 199–207.

      O. Ghashghaei, F. Seghetti & R. Lavilla (2019). Selectivity in multiple multicomponent reactions:

      types and synthetic applications. Beilstein journal of organic chemistry, 15(1), 521–534.

      O. Levenspiel, (1999). Chemical Reaction Engineering. Chapter 10. New York: John Wiley &

      Sons.

      P.J. Trambouze, E.L. Piret, (1959). Continuous stirred tank reactors: Designs for maximum conversions of

      raw material to desired product. Homogeneous reactions. AIChE Journal. 5(3). 384–390.

      W. L. Luyben (2007). Chemical reactor design and control. John Wiley & Sons.

      Downloads

      Published

      2020-11-30

      How to Cite

      Simulating Trambouze reaction for a series reactor. (2020). Malaysian Journal of Chemical Engineering and Technology, 3(1), 1-6. https://doi.org/10.24191/mjcet.v3i1.10930

      Similar Articles

      1-10 of 49

      You may also start an advanced similarity search for this article.

      Most read articles by the same author(s)