Intensive Column Apparatus for Chemical Reactions


A solution of the intensification problem of the column chemical reactors is presented in the approximation of the mechanics of continua. The effect of the radial non-uniformity of the velocity distribution, the effect of the tangential flow and simultaneous mass, and heat transfer processes are analyzed. A theoretical analysis of the simultaneous mass and heat transfer processes in column reactors is presented.

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Boyadjiev, C. , Doichinova, M. , Popova-Krumova, P. and Boyadjiev, B. (2014) Intensive Column Apparatus for Chemical Reactions. Open Access Library Journal, 1, 1-9. doi: 10.4236/oalib.1100413.

Conflicts of Interest

The authors declare no conflicts of interest.


[1] Boyadjiev, Chr. (2006) Diffusion Models and Scale-Up. International Journal of Heat and Mass Transfer, 49, 796-799.
[2] Boyadjiev, Chr. (2009) Modeling of Column Apparatuses. Transactions of Academenergo, 3, 7-22.
[3] Boyadjiev, Chr. (2010) Theoretical Chemical Engineering. Modeling and Simulation. Springer-Verlag, Berlin Heidelberg, 594.
[4] Doichinova, M. and Boyadjiev, Chr. (2012) On the Column Apparatuses Modeling. International Journal of Heat and Mass Transfer, 55, 6705-6715.
[5] Lietuvos Respublika (1994) Patent No. 3884.
[6] Boyadjiev, Chr., Boyadjiev, B., Doichinova, M. and Popova-Krumova, P. (2013) Column Reactor for Chemical Processes. Utility Model, Application Number 2464.

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