The head of water over the centre of an orifice of diameter 20 mm is 1 m. The actual discharge through the orifice is 0.85 litre/s. Find the coefficient of discharge.
0.61
This problem requires us to determine the coefficient of discharge for a small orifice given its diameter, the head of water above its center, and the actual discharge rate.
Find the coefficient of discharge, \( C_d \).
The coefficient of discharge \( C_d \) is defined as the ratio of the actual discharge \( Q_{\text{actual}} \) to the theoretical discharge \( Q_{\text{theoretical}} \):
\( C_d = \frac{Q_{\text{actual}}}{Q_{\text{theoretical}}} \)
The theoretical discharge \( Q_{\text{theoretical}} \) is the product of the theoretical velocity \( v_{\text{theoretical}} \) and the area of the orifice \( A \):
\( Q_{\text{theoretical}} = A \times v_{\text{theoretical}} \)
The theoretical velocity \( v_{\text{theoretical}} \) through the orifice under a head \( H \) is given by Torricelli's theorem:
\( v_{\text{theoretical}} = \sqrt{2gH} \)
Where \( g \) is the acceleration due to gravity (approximately \( 9.81 \) m/s²).
The area of the circular orifice \( A \) is given by:
\( A = \frac{\pi}{4}d^2 \)
First, let's convert the given values to consistent units (SI units):
Now, calculate the area of the orifice \( A \):
\( A = \frac{\pi}{4}d^2 = \frac{\pi}{4}(0.02 \text{ m})^2 = \frac{\pi}{4}(0.0004 \text{ m}^2) = \pi \times 0.0001 \text{ m}^2 \approx 0.000314159 \text{ m}^2 \)
Next, calculate the theoretical velocity \( v_{\text{theoretical}} \) using \( g = 9.81 \) m/s²:
\( v_{\text{theoretical}} = \sqrt{2gH} = \sqrt{2 \times 9.81 \text{ m/s}^2 \times 1 \text{ m}} = \sqrt{19.62 \text{ m}^2/\text{s}^2} \approx 4.42945 \text{ m/s} \)
Now, calculate the theoretical discharge \( Q_{\text{theoretical}} \):
\( Q_{\text{theoretical}} = A \times v_{\text{theoretical}} \approx (0.000314159 \text{ m}^2) \times (4.42945 \text{ m/s}) \approx 0.0013913 \text{ m}^3/\text{s} \)
Finally, calculate the coefficient of discharge \( C_d \):
\( C_d = \frac{Q_{\text{actual}}}{Q_{\text{theoretical}}} = \frac{0.85 \times 10^{-3} \text{ m}^3/\text{s}}{0.0013913 \text{ m}^3/\text{s}} = \frac{0.00085}{0.0013913} \approx 0.611 \)
Rounding the result to two decimal places, the coefficient of discharge is approximately \( 0.61 \).
| Parameter | Value |
|---|---|
| Orifice Diameter (\(d\)) | 0.02 m |
| Head of Water (\(H\)) | 1 m |
| Actual Discharge (\(Q_{\text{actual}}\)) | \(0.85 \times 10^{-3}\) m³/s |
| Theoretical Velocity (\(v_{\text{theoretical}}\)) | \(\approx 4.429\) m/s |
| Orifice Area (\(A\)) | \(\approx 0.000314\) m² |
| Theoretical Discharge (\(Q_{\text{theoretical}}\)) | \(\approx 0.00139\) m³/s |
| Coefficient of Discharge (\(C_d\)) | \(\approx 0.61\) |
The calculated coefficient of discharge is approximately 0.61.
| Term | Definition/Formula |
|---|---|
| Orifice | An opening, typically small compared to the cross-sectional area of the container, through which fluid flows. |
| Head of Water (\(H\)) | The vertical distance between the free surface of the liquid and the center of the orifice. |
| Theoretical Velocity (\(v_{\text{theoretical}}\)) | The velocity of flow through the orifice assuming no losses. Based on Torricelli's theorem: \(v_{\text{theoretical}} = \sqrt{2gH}\). |
| Theoretical Discharge (\(Q_{\text{theoretical}}\)) | The discharge calculated assuming the entire orifice area is effective and the velocity is theoretical: \(Q_{\text{theoretical}} = A \times v_{\text{theoretical}}\). |
| Actual Discharge (\(Q_{\text{actual}}\)) | The measured discharge through the orifice, which is always less than the theoretical discharge due to losses and contraction of the jet. |
| Coefficient of Discharge (\(C_d\)) | The ratio of actual discharge to theoretical discharge: \(C_d = Q_{\text{actual}} / Q_{\text{theoretical}}\). It accounts for velocity losses and jet contraction. |
The coefficient of discharge \( C_d \) is a crucial parameter for real-world fluid flow calculations through orifices. It accounts for two main factors:
The coefficient of discharge is related to the coefficient of contraction and the coefficient of velocity by the equation:
\( C_d = C_c \times C_v \)
For a sharp-edged orifice, typical values are \( C_c \approx 0.60 \) to \( 0.65 \), \( C_v \approx 0.95 \) to \( 0.99 \), resulting in \( C_d \approx 0.57 \) to \( 0.65 \). The calculated value of 0.61 in this problem falls within the typical range for \( C_d \).
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