Heat Transfer Handbook part 4 ppt

... 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], (22) Lines: ... 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 33...

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... 147 4 / 2nd Proofs / Heat Transfer Handbook / Bejan 147 4 SUBJECT INDEX 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 [ 147 4], ... arrays, 49 5 49 7 flush-mounted heat sources, 49 1 49 2 forced convection external flows from, 49 0–500 isolated blocks, 49 3 49 5 objects on, 44 4, 49 0–5...

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... 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], ... 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 28 29 30...

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... 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] , ... / 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 4...

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... / Page 49 / 2nd Proofs / Heat Transfer Handbook / Bejan 49 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 [49 ], (7) Lines: ... Page 45 / 2nd Proofs / Heat Transfer Handbook / Bejan INTRODUCTION 45 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...

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... 0.19 74 0 .44 03 0.6 745 0.9066 1. 148 1 1 .44 78 s (vap.) 4. 4165 3.6795 3.2 149 2.9067 2.6920 2.5357 2 .41 65 2.3190 2.22 94 2.1279 1. 945 1 c v (liq.) 1.6012 1.5 345 1 .46 47 1 .42 82 1 .41 84 1 .42 81 1 .45 36 1 .49 41 ... 2. 140 4 2.3118 2.8 546 c p (liq.) 3 .40 84 3 .46 92 3. 549 3 3.6580 3.8129 4. 047 4 4. 43 54 5.1872 7.2923 11.109 94. 012 c p (vap.) 2. 145 8 2.2053 2.2930 2...

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... / Heat Transfer Handbook / Bejan 110 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 [110], (68) Lines: 22 74 to 2297 ——— * 528.0pt ... (liq.) 0.8686 0. 948 8 1.0262 1.10 14 1.1 748 1.2110 1. 247 1 1.2833 1.3199 1.3579 1.3995 s (vap.) 1.3 940 1 .40 78 1 .42 58 1 .44 61 1 .46 71 1 .47 73 1 .48...

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... / 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 ], ... 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 [ 244 ], ( 84)...

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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 [2 74] , ( 14) Lines: 635 to 6 64 ——— 1.00616pt PgVar ——— Normal Page * PgEnds: Eject [2 74] , ( 14) where Q is the total heat transfer ... RESISTANCES 271 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 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 [2 94] , ( 34) Lines: 144 0 to 147 6 ——— 5.87788pt PgVar ——— Long Page PgEnds: T E X [2 94] , ( 34) dimensionless system parameters ( = a/b, ... Handbook / Bejan 292 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...

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