Heat Transfer Handbook part 10 pdf

... 489.70 440.25 391.49 343.00 294 .10 243.92 218.04 191.41 163.77 134.40 w (vap.) 112.77 112.19 110. 92 108 .86 105 .91 101 .93 96.707 93.543 89.944 85.845 81.148 σ 0. 0104 0.0089 0.0075 0.0061 0.0048 ... 54.371 109 .88 h (liq.) −334.31 −221.69 100 .87 −35.064 35.664 112.27 195.83 287.71 390.11 507.42 656.91 h (vap.) 955.68 101 3.1 106 5.3 108 9.5 1111.6 1129.6 1140.4 1140.3 1129.3 1117...

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... PROPERTIES 151 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 [151], (109 ) Lines: 3693 to 3703 ——— * 24.75998pt PgVar ——— Normal Page * PgEnds: PageBreak [151], (109 ) BOOKCOMP, Inc. — John Wiley & Sons / Page 153 / 2nd Proofs / Heat Transfer Handbook ... MATERIALS 1 2 3 4 5 6 7 8 9 10 11 12 13 14 1...

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... q 1 2πh 1 r 1 L (3.90) BOOKCOMP, Inc. — John Wiley & Sons / Page 190 / 2nd Proofs / Heat Transfer Handbook / Bejan 190 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 [190], ... generation. BOOKCOMP, Inc. — John Wiley & Sons / Page 186 / 2nd Proofs / Heat Transfer Ha...

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... 1.00 010 a 2 1.5056 1.5150 1. 5101 a 3 0.35931 0.37302 0.38637 a 4 39.66 68.59 115.91 a 5 0.31604 0.31538 0.31529 BOOKCOMP, Inc. — John Wiley & Sons / Page 289 / 2nd Proofs / Heat Transfer Handbook ... John Wiley & Sons / Page 284 / 2nd Proofs / Heat Transfer Handbook / Bejan 284 THERMAL SPREADING AND CONTACT RESISTANCES 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19...

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... These results are valid in the range 10 4 ≤ Re D h ≤ 10 6 and 10 6 ≤ Re L ≤ 10 8 , which can be shown to correspond to the pressure drop number range 10 11 ≤ Be ≤ 10 16 . 5.9 SUMMARY OF FORCED CONVECTION ... Eject [422], (28) 0.05 0.04 0.04 0.000,01 0.000,05 0.0001 0.0002 0.0004 0.0006 0.001 0.002 0.004 0.008 0.01 0.015 0.02 0.006 0.0008 Relative roughness, /Dk s 0.01 0.02 0.03 0....

Ngày tải lên: 05/07/2014, 16:20

... John Wiley & Sons / Page 465 / 2nd Proofs / Heat Transfer Handbook / Bejan HEAT TRANSFER FROM SINGLE OBJECTS IN UNIFORM FLOW 465 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 [465], ... John Wiley & Sons / Page 463 / 2nd Proofs / Heat Transfer Handbook / Bejan HEAT TRANSFER FROM SINGL...

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... John Wiley & Sons / Page 479 / 2nd Proofs / Heat Transfer Handbook / Bejan HEAT TRANSFER FROM SINGLE OBJECTS IN UNIFORM FLOW 479 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 [479], ... John Wiley & Sons / Page 481 / 2nd Proofs / Heat Transfer Handbook / Bejan HEAT TRANSFER FROM SINGL...

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... 16 100 0.90 0.40 Staggered 1.6–40 1.04 0.40 Aligned 100 100 0 0.52 0.50 Staggered 40 100 0 0.71 0.50 Aligned (S T /S L > 0.7) 100 0–2 × 10 5 0.27 0.63 Staggered (S T /S L < 2) 100 0–2 × 10 5 0.35 ... (S T /S L > 2) 100 0–2 × 10 5 0.40 0.60 Aligned 2 10 5 –2 10 6 0.033 0.80 Staggered (Pr > 0.70) 2 10 5 –2 10 6 0.031 (S T /S L ) 0.20 0.80 Staggered (Pr = 0.70) 2 10 5...

Ngày tải lên: 05/07/2014, 16:20

... 0.7, 1.0, 10. 0, 100 .0, and ∞, respectively. BOOKCOMP, Inc. — John Wiley & Sons / Page 546 / 2nd Proofs / Heat Transfer Handbook / Bejan 546 NATURAL CONVECTION 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 [546], ... q  is the constant heat flux input imposed at BOOKCOMP, Inc. — John Wiley & S...

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... John Wiley & Sons / Page 589 / 2nd Proofs / Heat Transfer Handbook / Bejan RADIATIVE PROPERTIES OF SOLIDS AND LIQUIDS 589 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 [589], ... there BOOKCOMP, Inc. — John Wiley & Sons / Page 584 / 2nd Proofs / Heat Transfer Handbook / Bejan 584 THERMAL RADI...

Ngày tải lên: 05/07/2014, 16:20