- From equation (4.44) for S/q1/50.1919 (0.16),
C0.72260.743 log 0.19190.18919%, ya0.320 m.
From equation (4.45) for S/q2/30.100.23 (outside experimental
limit),
C0.5027(0.10)0.3850.20721%, ya0.328 m.
The equivalent roughness k 2 ais obtained from (Section 8.2.2)
R
n
1/6
18 log
with
0.16 104 m,
a3.423 104.
Thus a# /7, i.e. the flow regime is hydraulically rough with
k0.7 mm. (Note that kis smaller than the 1.2 mm applicable to
Anderson’s experiments; also, equation (4.44) underestimates Cby
about 0.1 for very low values of S/q1/5when compared with actual
experimental results.)
As explained in Section 4.7.3 in the above computations (1–3) the
uniform flow depth for the water component in the water–air
mixturey 0 should have been used instead of y 0. On the other hand
forCabout 0.3 the difference between these two values is negligible
(from Straub and Anderson y 0 /y 0 0.98).
- From equation (4.52) with 14° (Stan0.25) C21%. As
n^28 g/R1/3, for non-aerated flow 0.0191 and from equation (4.43)
a0.0191 (1 1.190.21^2 )0.0175.
From the Darcy–Weisbach equation y 0 ^2 R 0 Q^2 a/b^28 gS0.0125 and
y 0 0.25 m (giving y 0 /y 0 0.965 and ya0.25/(1 0.21)0.316 m.
The aerated flow velocity is V3.75/0.2515.0 m s^1 (14.48).
Using equation (4.53) C0.75(sin 14)0.7526%.
- From equation (4.50), for K 2 q/b3.75 m s^1. By trial and error,
V19.45 m s^1 (velocity of aerated flow).
c 1 0.006 1.1241.
Thusya2.124y 0 0.550 m; C 1 (0.259/0.550)53%.
ya
y 0
19.45^2
9.810.206
V^2
gR
(^11)
(^1)
0.16 104
7
11.6 106
(gRS)1/2
11.6v
U*
6 R
a /7