Heat Transfer Handbook part 6 ppt

... ASME, 66 , 67 1 68 4. Rohsenow, W. M. (1952). A Method for Correlation Heat Transfer Data for Surface Boiling in Liquids, Trans. ASME, 74, 969 –975. Rohsenow, W. M., and Choi, H. Y. (1 961 ). Heat Mass ... Sons / Page 46 / 2nd Proofs / Heat Transfer Handbook / Bejan 46 THERMOPHYSICAL PROPERTIES OF FLUIDS AND MATERIALS 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21...

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... 959, 960 Vertical tubes: flow boiling in, 66 3 66 4, 66 6, 67 1 67 9 Chen correlation, 67 2 67 3 Gungor—Winterton correlation, 67 4– 67 5 horizontal tube correlations based on, 67 9 68 0 Shah correlation, 67 3 67 4 Steiner—Taborek ... 60 8 60 9 direct integration, 60 0, 60 6 reciprocity rule, 60 7 summation rule, 60 6 60 7 view factor algebra, 60 7 60 8 thermal radiation, 60 0...

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... 9 / 2nd Proofs / Heat Transfer Handbook / Bejan HEAT TRANSFER FUNDAMENTALS 9 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 [9], ... 7 / 2nd Proofs / Heat Transfer Handbook / Bejan HEAT TRANSFER FUNDAMENTALS 7 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...

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... Page 22 / 2nd Proofs / Heat Transfer Handbook / Bejan 22 BASIC CONCEPTS 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 [22], ... 27 / 2nd Proofs / Heat Transfer Handbook / Bejan CONSERVATION OF ENERGY 27 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...

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... Page 34 / 2nd Proofs / Heat Transfer Handbook / Bejan 34 BASIC CONCEPTS 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 [34], ... 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...

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... 10 −7 0.0002 0.00 76 0.0 266 0.0732 0. 168 5 0.33 96 0 .61 77 1.0384 1 .64 29 2.48 36 ρ (liq.) 7 56. 28 711.19 66 6.32 64 3.13 61 8.95 593.35 565 .69 535.02 499.73 4 56. 47 395.85 ρ (vap.) 0.0000 0.00 86 0. 265 1 0.8533 ... 119.80 h (liq.) −49 .64 8 −3. 466 5 44 .68 0 95.083 148.13 204.27 264 .00 327. 86 3 96. 67 472 .64 566 .69 h (vap.) 404.10 431.22 460 . 56 491.72 524.22 557.51 5...

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... 2.2820 w (liq.) 65 4 .66 579.81 504.72 430.19 355. 56 317.77 279.32 239.80 198 .61 154.70 105.83 w (vap.) 101. 56 103.78 104 .61 103 .64 100.37 97 .66 8 94.081 89.431 83.4 56 75.752 65 .65 8 η (liq.) 5 06. 03 375.90 ... 287.28 222 .61 172 .66 151.41 131.94 113.78 96. 438 79. 162 60 .232 η (vap.) 9.1935 9.9598 10 .69 7 11.458 12.270 12.721 13.232 13.844 14 .63 8 15.803 17.9 76 λ (liq.)...

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... / Page 2 46 / 2nd Proofs / Heat Transfer Handbook / Bejan 2 46 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 [2 46] , ... 248 / 2nd Proofs / Heat Transfer Handbook / Bejan 248 CONDUCTION HEAT TRANSFER 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 2...

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... RESISTANCES 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 [274], (14) Lines: 63 5 to 66 4 ——— 1.0 061 6pt PgVar ——— Normal ... 0 .6 0.9028 0.1 0.9975 0.7 0. 863 0 0.2 0.9899 0.8 0.81 26 0.3 0.9771 0.9 0.7459 0.4 0.9587 1.0 0 .63 66 0.5 0.9342 BOOKCOMP, Inc. — John Wiley & Sons / Page 279 / 2nd Pro...

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... Proofs / Heat Transfer Handbook / Bejan 2 96 THERMAL SPREADING AND CONTACT RESISTANCES 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 [2 96] , ... Proofs / Heat Transfer Handbook / Bejan 298 THERMAL SPREADING AND CONTACT RESISTANCES 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 2...

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