Heat Transfer Handbook part 10 pdf
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...
Heat Transfer Handbook part 17 pdf
... PROPERTIES
151
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[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
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Heat Transfer Handbook part 20 pdf
... 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
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[190], ... generation.
BOOKCOMP, Inc. — John Wiley & Sons / Page 186 / 2nd Proofs / Heat Transfer Ha...
Heat Transfer Handbook part 30 pdf
... 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
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19...
Heat Transfer Handbook part 44 pdf
... 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....
Heat Transfer Handbook part 48 pdf
... John Wiley & Sons / Page 465 / 2nd Proofs / Heat Transfer Handbook / Bejan
HEAT TRANSFER FROM SINGLE OBJECTS IN UNIFORM FLOW
465
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[465], ... John Wiley & Sons / Page 463 / 2nd Proofs / Heat Transfer Handbook / Bejan
HEAT TRANSFER FROM SINGL...
Heat Transfer Handbook part 49 pdf
... John Wiley & Sons / Page 479 / 2nd Proofs / Heat Transfer Handbook / Bejan
HEAT TRANSFER FROM SINGLE OBJECTS IN UNIFORM FLOW
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[479], ... John Wiley & Sons / Page 481 / 2nd Proofs / Heat Transfer Handbook / Bejan
HEAT TRANSFER FROM SINGL...
Heat Transfer Handbook part 50 pdf
... 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...
Heat Transfer Handbook part 56 pdf
... 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
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[546], ... q
is the constant heat flux input imposed at
BOOKCOMP, Inc. — John Wiley & S...
Heat Transfer Handbook part 60 pdf
... John Wiley & Sons / Page 589 / 2nd Proofs / Heat Transfer Handbook / Bejan
RADIATIVE PROPERTIES OF SOLIDS AND LIQUIDS
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[589], ... there
BOOKCOMP, Inc. — John Wiley & Sons / Page 584 / 2nd Proofs / Heat Transfer Handbook / Bejan
584 THERMAL RADI...
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