A strip-intermittent combined stirrer is developed for mixing viscous fluids in order to intensify heat and mass transfer. The stirrer’s optimum structural features (number of turns and strip width) are determined from experimental results and a dependence is plotted for power factor on modified Reynolds criterion K N = f(Re M ).
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References
Yu. I. Dytnerskii, Processes and Equipment for Chemical Technology: Textbook, Part 1, Theoretical Bases of Chemical Technology. Hydromechanical and Thermal Processes and Equipment, Khimiya, Moscow (1995), 2nd ed.
A. G. Kasatkin, Basic Processes and Chemical Technology Equipment, Alians, Moscow (2009), 15th ed.
GOST 22577−77, Mixing Devices for Liquid and Inhomogeneous Fluids Terms and Determination (1978).
L. N. Braginskii, V. I. Begachev, and V. I. Barabash, Mixing in Liquid Media, Moscow (1984).
I. A. Gorlovskii and N. A. Kozulin, Paint Industry Plant Equipment: Textbook, Khimiya, Leningrad (1980), 3rd ed.
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Translated from Khimicheskoe i Neftegazovoe Mashinostroenie, No. 5, pp. 13–14, May, 2015.
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Leont’ev, V.K., Korableva, O.N. Development of a Combined Stirrer for Mixing Viscous Fluids. Chem Petrol Eng 51, 308–310 (2015). https://doi.org/10.1007/s10556-015-0043-y
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DOI: https://doi.org/10.1007/s10556-015-0043-y