Heat Transfer Handbook part 1 docx

... Proofs / Heat Transfer Handbook / Bejan 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 [ -11 ], (5) Lines: 10 2 to 203 ——— * 22.60799pt ... Proofs / Heat Transfer Handbook / Bejan 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...

Ngày tải lên: 05/07/2014, 16:20

... 439.04 443 .11 445.66 s (liq.) 0.9408 1. 03 01 1 .11 54 1. 1977 1. 2780 1. 317 5 1. 3570 1. 3964 1. 4362 1. 4768 1. 519 3 s (vap.) 1. 611 2 1. 618 8 1. 6308 1. 6453 1. 6609 1. 6686 1. 6759 1. 6824 1. 6878 1. 6 914 1. 6 917 c v (liq.) ... 0.7738 0.86 21 0.9463 1. 0275 1. 1064 1. 1454 1. 18 41 1.2229 1. 26 21 1.30 21 1.34 41 s (vap.) 1. 4375 1. 4394 1. 4485 1...

Ngày tải lên: 05/07/2014, 16:20

... Proofs / Heat Transfer Handbook / Bejan 240 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 [240], ... Proofs / Heat Transfer Handbook / Bejan 236 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...

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... 2 61 / 2nd Proofs / Heat Transfer Handbook / Bejan 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 [First Page] [2 61] , (1) Lines: ... / Heat Transfer Handbook / Bejan 270 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...

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... Sons / Page 3 41 / 2nd Proofs / Heat Transfer Handbook / Bejan CONFORMING ROUGH SURFACE MODELS 3 41 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 [3 41] , ... / Heat Transfer Handbook / Bejan 348 THERMAL SPREADING AND CONTACT RESISTANCES 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 1...

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... Proofs / Heat Transfer Handbook / Bejan SUMMARY OF HEAT TRANSFER CORRELATIONS 513 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 [ 513 ], ... Page 515 / 2nd Proofs / Heat Transfer Handbook / Bejan NOMENCLATURE 515 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20...

Ngày tải lên: 05/07/2014, 16:20

... 2,3 c 00 ···c N0 −2. 211 8 1. 1987 −0.035596 −3.9893 −2.7669 −2 .10 81 −0.3 916 3 . . . . . . . . . −0.85667 −0.93048 −0 .14 3 91 1. 2 710 1. 1090 1. 019 5 −0. 218 97 c 0M ···C NM −0 .10 838 −0 .17 156 −0.045 915 −0.23678 −0 .19 7 31 ... Page 615 / 2nd Proofs / Heat Transfer Handbook / Bejan RADIATIVE PROPERTIES OF PARTICIPATING MEDIA 615 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15...

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... Bejan POST-DRYOUT HEAT TRANSFER 6 91 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 [6 91] , (57) Lines: 19 69 to 19 71 ——— 3.42099pt ... Proofs / Heat Transfer Handbook / Bejan POST-DRYOUT HEAT TRANSFER 689 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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... Proofs / Heat Transfer Handbook / Bejan FILM CONDENSATION ON TUBE BUNDLES 769 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 [769], ... / 2nd Proofs / Heat Transfer Handbook / Bejan 766 CONDENSATION 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 818 / 2nd Proofs / Heat Transfer Handbook / Bejan 818 HEAT EXCHANGERS 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 [ 818 ], ... Bejan HEAT EXCHANGER ANALYSIS METHODS 815 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 3...

Ngày tải lên: 05/07/2014, 16:20