Discharge through an external mouthpiece — practical formula Let a be the cross-sectional area of the external mouthpiece and H the head above its centerline. The discharge Q is approximately:
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AQ = 0.855 * a * sqrt(2 * g * H)
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BQ = 1.855 * a * sqrt(2 * g * H)
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CQ = 0.585 * a * sqrt(2 * g * H)
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DQ = 0.855 * a * (2 * g * H)
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EQ = a * sqrt(2 * g * H) (coefficient = 1.00)
Answer
Correct Answer: Q = 0.855 * a * sqrt(2 * g * H)
Explanation
Introduction / Context:Mouthpieces are short tubes fitted at tank orifice openings. For a well-designed external mouthpiece running full, empirical studies give a practical coefficient close to 0.855 for the discharge relation.
Given Data / Assumptions:
- External (protruding) mouthpiece of short length.
- Steady incompressible flow; fully aerated jet; negligible approach velocity.
- Coefficient of discharge C_d ≈ 0.855 (typical value).
Concept / Approach:Ideal discharge from Bernoulli/continuity is Q_ideal = a * sqrt(2 * g * H). Real discharge is Q = C_d * Q_ideal with C_d < 1 to account for contraction and losses through the mouthpiece.
Step-by-Step Solution:
Write ideal flow: Q_ideal = a * sqrt(2 g H).Apply coefficient: Q = C_d * a * sqrt(2 g H).Use C_d ≈ 0.855 for external mouthpiece → Q ≈ 0.855 a sqrt(2 g H).Verification / Alternative check:Compare to sharp-edged orifice (C_d ≈ 0.62): the mouthpiece tends to have a higher C_d when running full because it controls contraction and reduces separation.
Why Other Options Are Wrong:
- 1.855: too high; implies C_d > 1.
- 0.585: too low for a full, well-formed mouthpiece.
- 0.855 * a * (2 g H): missing the square root, wrong dimensions.
- Coefficient = 1: assumes ideal flow without losses.
Common Pitfalls:Mixing orifice and mouthpiece coefficients; forgetting the square-root dependence on head.
Final Answer:Q = 0.855 * a * sqrt(2 * g * H)