Heat Transfer Handbook part 118 ppt

... Uniform Heat Flux from the Side, Int. J. Heat Mass Transfer, 26, 1339–1346. Bejan, A. (1983b). Natural Convection Heat Transfer in a Porous Layer with Internal Flow Obstructions, Int. J. Heat Mass Transfer, ... 815–822. Bejan, A. (1984). Convection Heat Transfer, Wiley, New York. Bejan, A. (1987). Convective Heat Transfer in Porous Media, in Handbook of Single-Phase Conve...

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... 114 118 for mixtures, 117 118 Transverse high-fin heat exchangers, 868– 878 air-fin coolers, 871–875 bond/contact resistance of high-fin tubes, 870 fin efficiency approximation, 871 overall heat transfer ... gas isobaric heat capacity, 55–57 for mixtures, 113–114 physical constants and fixed points, 52–54 BOOKCOMP, Inc. — John Wiley & Sons / Page 1476 / 2nd Proofs / Heat Transfer...

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... Lumped-capacity heating and cooling 1.1.6 Convective heat transfer Heat transfer coefficient Dimensionless parameters Natural convection Forced convection 1.1.7 Phase-change heat transfer 1.1.8 ... Bejan 16. Heat Pipes 1181 Jay M. Ochterbeck 17. Heat Transfer in Manufacturing and Materials Processing 1231 Richard N. Smith, C. Haris Doumanidis, and Ranga Pitchumani 18. Micro...

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... within the control volume  =  net transfer of energy by fluid flow  +  net heat transfer by conduction  ×  rate of internal heat generation  −    net work transfer from the control volume ... conductivity k, neglible viscous dissipation Φ, zero internal heat BOOKCOMP, Inc. — John Wiley & Sons / Page 24 / 2nd Proofs / Heat Transfer Handbook / Bejan 24 BASIC CONCEP...

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... current are not used in a study of heat transfer and are not considered further. BOOKCOMP, Inc. — John Wiley & Sons / Page 35 / 2nd Proofs / Heat Transfer Handbook / Bejan UNITS 35 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [35], ... Factors for Heat Transfer Parameters from English Engineerin...

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... A Method for Correlation Heat Transfer Data for Surface Boiling in Liquids, Trans. ASME, 74, 969–975. Rohsenow, W. M., and Choi, H. Y. (1961). Heat Mass and Momentum Transfer, Prentice-Hall, Englewood ... values for many properties BOOKCOMP, Inc. — John Wiley & Sons / Page 48 / 2nd Proofs / Heat Transfer Handbook / Bejan 48 THERMOPHYSICAL PROPERTIES OF FLUIDS AND MATERIALS 1...

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... BOOKCOMP, Inc. — John Wiley & Sons / Page 62 / 2nd Proofs / Heat Transfer Handbook / Bejan 62 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [62], ... 539.23 548.17 546.52 512.98 BOOKCOMP, Inc. — John Wiley & Sons / Page 67 / 2nd Proofs / Heat Transfer Handbook / Bejan 67 1 2 3 4 5 6 7 8 9 10 11...

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... gives values of the ideal gas isobaric heat capacity for BOOKCOMP, Inc. — John Wiley & Sons / Page 118 / 2nd Proofs / Heat Transfer Handbook / Bejan 118 THERMOPHYSICAL PROPERTIES OF FLUIDS ... T T crit 0 T crit j θ(T , ρ) (2.39) BOOKCOMP, Inc. — John Wiley & Sons / Page 111 / 2nd Proofs / Heat Transfer Handbook / Bejan THERMOPHYSICAL PROPERTIES OF FLUIDS 111 1 2 3 4...

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... equation BOOKCOMP, Inc. — John Wiley & Sons / Page 242 / 2nd Proofs / Heat Transfer Handbook / Bejan 242 CONDUCTION HEAT TRANSFER 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 [242], ... (3.342) BOOKCOMP, Inc. — John Wiley & Sons / Page 248 / 2nd Proofs / Heat Transfer Handbook / Bejan 248...

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... transient heat transfer rate: Q =  A q n dA =  A −k ∂T ∂n dA (W) (4.17) where q n is the heat flux component normal to the area and ∂T /∂n is the temperature gradient normal to the area. If the heat ... in planes z =   √ A t BOOKCOMP, Inc. — John Wiley & Sons / Page 277 / 2nd Proofs / Heat Transfer Handbook / Bejan SPREADING AND CONSTRICTION RESISTANCES IN AN ISOTROPIC...

Ngày tải lên: 05/07/2014, 16:20