Page 162 - Design and Operation of Heat Exchangers and their Networks
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150 Design and operation of heat exchangers and their networks
10 7
10 6
III IV
10 5
10 4 II
V VI
a (W/m 2 K) 10 3 2 I
10
Boiling curve
10
1
0.1
0.01
0.01 0.1 1 10 10 2 10 3 10 4
Δt (K)
10 7
III IV
V VI
10 6
10 5
II
10 4
q (W/m 2 ) 10 3 2 I
Boiling curve
10
10
1
0.1
0.01
0.01 0.1 1 10 10 2 10 3 10 4
Δt (K)
Fig. 4.1 Nukiyama boiling curve with data of Farber and Scorah (1948).
