Abstract
The new approach for the modeling of the processes in column apparatuses (Boyadjiev in Theoretical chemical engineering. Modeling and simulation. Springer, Berlin, Heidelberg, 2010, [1]; Doichinova, Boyadjiev in Int J Heat Mass Transf 55:6705–6715, 2012, [2]; Boyadjiev in Pure Appl Math Adv Appl 10(2):131–150, 2013 [3]) presents the convection–diffusion and average-concentration models of the column chemical reactors (in Chaps. 2 and 5), where the radial velocity component is equal to zero in the cases of a constant axial velocity radial non-uniformity along the column height:
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References
Boyadjiev C (2010) Theoretical chemical engineering. Modeling and simulation. Springer, Berlin, Heidelberg
Doichinova M, Boyadjiev C (2012) On the column apparatuses modeling. Int J Heat Mass Transf 55:6705–6715
Boyadjiev C (2013) A new approach for the column apparatuses modeling in chemical engineering. J Pure Appl Math Adv Appl 10(2):131–150
Boyadjiev B, Boyadjiev C (2017) New models of industrial column chemical reactors. Bul Chem Commun 49(3):706–710
Boyadjiev B, Boyadjiev C (2018) A new approach to modeling of chemical processes in industrial column apparatuses. Chem Eng Tech (in press)
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Boyadjiev, C., Doichinova, M., Boyadjiev, B., Popova-Krumova, P. (2018). Industrial Column Chemical Reactors. In: Modeling of Column Apparatus Processes. Heat and Mass Transfer. Springer, Cham. https://doi.org/10.1007/978-3-319-89966-4_10
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DOI: https://doi.org/10.1007/978-3-319-89966-4_10
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