Table 5. Characteristics of micro-fin tube designs.
α
β
e*
( )
( )
Design
(mm)
p/e
n
A/Ap
wt /wtp
h/hp
Original
0.15
2.14
25
90
65
1.28
1.22
1.8
EX
0.20
2.32
18
53
60
1.51
1.19
2.4
HEX
0.20
2.32
18
40
60
1.60
1.19
2.5
HEX-C
0.25
2.32
30
40
60
1.73
1.28
3.1
*e = fin height in mm, p = fin pitch, α = helix angle, β = included angle of fin cross-section,
n = number of fins in the tube, A = surface area of micro-fin tube, Wt = weight of the tube,
h = condensation heat transfer coefficient, and the subscript p denotes the corresponding
values for the plain tube.
Yasuda et al. (1990), shows the cross-sections of different micro-fin tubes. Table 5 gives
information on geometry, weight, enhancement ratio (for condensation of R-22) for the
four micro-fin tube designs (tube outside diameter = 9.52 mm).
The last column of Table 5 shows that the original micro-fin tube improves the conden-
sation coefficient for R-22 by 80% over a plain tube. The subsequent designs, EX and HEX,
raise the improvement figure to 140 and 150%, respectively. The HEX-C gives the highest
performance with an improvement of 210% over a plain tube. The improved designs have
greater fin heights (e) and smaller fin included angles (β). Condensation experiments with
micro-fin tubes conducted by Shinohara and Tobe (1985), Shinohara et al. (1987), and
Schlager et al. (1990c) have shown that the heat transfer coefficient for R-22 gradually
increases with helix angle (α), from 7, up to 30. Although these results do not clearly
identify the optimum helix angle (α), it does appear that α = 30 results in the best conden-
sation performance.
Figure 28 shows the R-22 condensation heat transfer coefficient as a function of mass
flux (velocity) for the tube geometries in Table 5, and demonstrates graphically the
superiority of micro-fin tubes over plain tubes. The HEX-C design stands out as distinctly
superior to HEX and EX designs for R-22 condensation. The tube outside diameter ap-
pears to have little effect on the heat transfer performance.
9.52 mm o.d.
7.54
10
HEX-C
HEX
EX
Plain
1
Figure 28. Heat transfer coefficient for R-22
100
200
300
400
500 600
condensing in micro-fin tubes.
2 s))
2
G,,Mass Velocitty((kgm / s
G Mass Velociy kg//m
44