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K. Knaebel (1993)
Pressure swing adsorption
G.K. Boreskov, Yu.Sh. Matros, O.V. Kiselev, G.A. Bunimovich (1977)
Implementation of heterogeneous catalytic process under the stationary modeDokl. AN SSSR, 237
Yu.I. Aristov, I.V. Mezentsev, V.A. Mukhin (2006)
New approach to regeneration of heat and moisture in the system of room ventilation. 1. Laboratory prototype of a regeneratorJ. Engng. Phys. Thermophys., 79
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Thermal Physics of Devices for Heat Utilization in Systems of Heat SupplyAir Ventilation and Conditioning
Yu.I. Aristov, I.V. Mezentsev, V.A. Mukhin (2006)
New approach to regeneration of heat and moisture in the system of room ventilation. 2. Prototype of a real deviceJ. Engng. Phys. Thermophys., 79
O. Levenspiel (1972)
Chemical Reaction Engineering
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Diffusion and heat transfer in chemical kinetics
T. Schumann (1929)
Heat transfer: A liquid flowing through a porous prismJournal of The Franklin Institute-engineering and Applied Mathematics, 208
Experimental results on reversing non-stationary heat transfer are presented for filtration of an air flow through an immobile heat accumulating medium consisting of lead (D = 2.0, 3.5, and 4.5 mm) and glass (D = 3.2 mm) balls. The studied device imitated the cyclic modes of heat regeneration in the ventilation system for domestic and office rooms. Dependency between the time of flow switching and Re number was measured. The mathematical model describing heat transfer between a gas flow and an immobile layer of balls was developed. Good correspondence between the experimental data and calculation results is observed for high Reynolds numbers. For low Re numbers the effect of heat losses is considerable, and experimental time of flow switching is shorter than the calculation one.
Thermophysics and Aeromechanics – Springer Journals
Published: Sep 1, 2006
Keywords: Heat Transfer; Heat Transfer Coefficient; Half Cycle; Pressure Swing Adsorption; Heat Regeneration
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