Establish the stage (headwater level)–discharge relationship for a concrete rectangular box culvert, using the following data: width = 1.2 m; height = 0.6 m; length = 30 m; slope = 1 in 1000; Manning’s n = 0.013; square-edged entrance conditions; free jet outlet flow; range of head water level for investigation =0–3 m; neglect the velocity of approach.
1. H/D ≤1.2. For H<0.6 m, free flow open-channel conditions prevail. Referring to Fig. 10.6 and assuming that a steep slope entry gives entrance control, i.e. the depth at the inlet is critical, for H = 0.2 m, ignoring entry loss y_{ c }=(2 / 3) \times 0.2=0.133\, m \text { and } V_{ c }=1.142 \,m s ^{-1} . This gives the critical slope (V n)^2 / R^{4 / 3}=0.00424 . Therefore the slope of the culvert is mild and hence subcritical flow analysis gives the following results:
\begin{aligned} Q & =1.2 y_0\left[1.2 y_0 /\left(1.2+2 y_0\right)\right]^{2 / 3}(0.001)^{1 / 2} / 0.013 \\ & =2.92 y_0\left[1.2 y_0 /\left(1.2+2 y_0\right)\right] ^{2 / 3} ; \end{aligned} (i)
Table 1
At the inlet over a short reach,
H=y_0+V^2 / 2 g+K_{ e } V^2 / 2 g . (ii)
The entrance loss coefficient, K_{ e } , is as follows:
for a square-edged entry, 0.5;
for a flared entry, 0.25;
for a rounded entry, 0.05;
Table 2
2. H/D≥1.2.
(a) For orifice flow
Q=C_{ d }(1.2 \times 0.6)[2 g(H-D / 2)]^{1 / 2} . (iii)
With C_{ d } = 0.62 the following results are obtained:
Table 3
(b) For pipe flow the energy equation gives
H+S_0 L=D+h_{ L }where
h_{ L }=K_{ e } V^2 / 2 g+(V n)^2 L / R^{4 / 3}+V^2 / 2 gThus
Q=2.08(H-0.57)^{1 / 2} (iv)
Table 4
During rising stages the barrel flows full from H = 0.72 m and during falling stages the flow becomes free-surface flow when H = 0.691 m.
The following table summarizes the results:
Table 5
Table 1
y_0(m) | Q\left(m^3 s^{-1}\right) (equation (i)) | y_c(m) |
0.2 | 0.165 | 0.124 |
0.4 | 0.451 | 0.243 |
0.6 (=D) | 0.785 | 0.352 |
Table 2
y_0(m) | H (m) (equation (ii)) | Q\left(m^3 s^{-1}\right) |
0.2 | 0.165 | 0.165 |
0.4 | 0.451 | 0.451 |
0.6 | 0.691 | 0.785 |
orifice ←> 0.6←(1.2 D = ) | 0.72 \longrightarrow | 0.817 (by interpolation) |
Table 3
H(m) | Q\left(m^3 s^{-1}\right) | y_{0} (m) (equation (i)) |
0.72 | 1.29 | > 0.6 → no orifice flow exists |
Table 4
H (m) Q\left(m^3 s^{-1}\right) (equation (iv)) | ||
y _0 \simeq 0.6(\text { equation }( i ) \leftarrow |
Table 5
H (m) | Q\left(m^3 s^{-1}\right) | Type of flow |
Rising stages | ||
0.236 | 0.165 | Open channel |
0.467 | 0.451 | Open channel |
0.691 | 0.785 | Open channel |
0.720 | 0.805 | Pipe flow |
1.00 | 1.364 | Pipe flow |
2.00 | 2.487 | Pipe flow |
3.00 | 3.242 | Pipe flow |
Falling stages | ||
2.00 | 2.487 | Pipe flow |
1.00 | 1.364 | Pipe flow |
0.72 | 0.805 | Pipe flow |
0.691 | 0.723 | Pipe flow |
0.691 | 0.785 | Open channel |
0.467 | 0.451 | Open channel |
0.236 | 0.165 | Open channel |