Time to cool a cryogenic object by a gaseous cryogenic agent |
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Authors: | S. P. Gorbachev A. A. Krikunov O. A. Goncharuk |
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Affiliation: | (1) Fortieth Anniversary of October Balashikhinsk Scientific-Production Combine of Cryogenic Machine Construction, USSR |
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Abstract: | Dependences to compute the cooling time of a single-channel object are obtained theoretically and confirmed experimentally.Notation D mass of helium in the channel - M mass of metal of the channel wall - G mass flow rate of the cryogenic agent - Gequ equivalent mass flow rate - cp, cm mean integrated specific heat of the cryogenic agent and the channel wall material - U perimeter - cooling time - 1 time of the first cooling period - T2 time of the second cooling period - channel wall temperature - T flow temperature - To initial flow temperature - Tin flow temperature at the channel input - W flow velocity - L channel length - Lin, Lout lengths of the delivery and removal pipelines - F, Fin, Fout cross-sectional areas of the channel being cooled, and of the delivery and removal pipelines - Fs total heat-transfer surface - d channel inner diameter - din, dout inner delivery and removal pipeline diameters - P flow pressure - P flow pressure at the input to the element - Pout flow pressure at the output from the element - Go, G1 initial and final flow rates of the cryogenic agent - z a coordinate - ¯z=z/L a dimensionless coordinate - dimensionless channel length - dimensionless cooling time - V1 dimensionless temperature - kG,a, ku, f, m, , g parameters - A, B constants - Re Reynolds number - R gas constant - coefficient of dynamic viscosity - hydraulic drag coefficient - coefficient of heat eliminationTranslated from Inzhenerno-Fizicheskii Zhurnal, Vol. 39, No. 4, pp. 629–635, October, 1980. |
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