Fluid mechanics and hydraulics miscellaneous
- A horizontal jet strikes a frictionless vertical plate (the plan view is shown in the figure). It is then divided into two parts, as shown in the figure. If the impact loss can be neglected, what is the value of θ ?
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Q2 = 1 + cosα Q1 1 - cosα
α-angle between plate and jet⇒ 0.75 = 1 + cosα 0.25 1 - cosα ⇒ 3 = 1 + cosα 1 - cosα
3 - 3cosα = 1 + cosα
2 = 4cosα⇒ cosα = 1 2
∴ α = 60°
φ = 90 - α = 30°Correct Option: B
Q2 = 1 + cosα Q1 1 - cosα
α-angle between plate and jet⇒ 0.75 = 1 + cosα 0.25 1 - cosα ⇒ 3 = 1 + cosα 1 - cosα
3 - 3cosα = 1 + cosα
2 = 4cosα⇒ cosα = 1 2
∴ α = 60°
φ = 90 - α = 30°
- A laboratory model of a river is built to a geometric scale of 1 : 00. The fluid used in the model is oil of mass density 900 kg/m3. The heighest flood in the river is 10,000 m3 / s. The corresponding discharge in the model shall be
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Apply Froude’s law.
Density of fluid does not affect model study.Qr = Qm = Lr5 / 2 Qp
Qp = 10000 m3 / sLr = 1 100 ⇒ Qm = 10000 × 1 5 / 2 100 = 10000 × 1 5 = 0.1 m3 / s 10 Correct Option: B
Apply Froude’s law.
Density of fluid does not affect model study.Qr = Qm = Lr5 / 2 Qp
Qp = 10000 m3 / sLr = 1 100 ⇒ Qm = 10000 × 1 5 / 2 100 = 10000 × 1 5 = 0.1 m3 / s 10
- For a two-dimensional irrotational flow, the velocity potential is defined as f = loge (x2 + y2). Which of the following is a possible stream function, Ψ , for this flow?
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We know,
∂Ψ = ∂φ ∂y ∂x = ∂ [ loge (x2 + y2) ] ∂x 1 d (x2 + y2) x2 + y2 dx = 1 × 2x x2 + y2
Integrating both sides,∫∂Ψ = ∫ 2x ∂y x2 + y2 ⇒Ψ = 2x. 1 tan-1 y + c x x ⇒Ψ = 2tan-1 y + c x Correct Option: C
We know,
∂Ψ = ∂φ ∂y ∂x = ∂ [ loge (x2 + y2) ] ∂x 1 d (x2 + y2) x2 + y2 dx = 1 × 2x x2 + y2
Integrating both sides,∫∂Ψ = ∫ 2x ∂y x2 + y2 ⇒Ψ = 2x. 1 tan-1 y + c x x
We know,⇒Ψ = 2tan-1 y + c x ∂Ψ = ∂φ ∂y ∂x = ∂ [ loge (x2 + y2) ] ∂x 1 d (x2 + y2) x2 + y2 dx = 1 × 2x x2 + y2
Integrating both sides,∫∂Ψ = ∫ 2x ∂y x2 + y2 ⇒Ψ = 2x. 1 tan-1 y + c x x ⇒Ψ = 2tan-1 y + c x
- A pump can lift water at a discharge of 0.15 m3 /s to a head of 25 m. The critical cavitation number (σc) for the pump is found to be 0.144. The pump is to be installed at a location where the barometric pressure is 9.8 m of water and the vapour pressure of water is 0.30 of water. The intake pipe friction loss is 0.40 m. Using the minimum value of NPSH (Net Positive Suction Head), the maximum allowable elevation above the sump water surface at which the pump can be located is
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σc = NPSH H ⇒ 0.144 = NPSH 25
∴ NPSH = 3.6 m
NPSH = Hatm - hv - hs - h2
Patm = Hatm = 9.8 m of water
Pv = Hv = 0.3 m of water
h2 = 0.4
⇒ 3.6 = 9.8 – 0.3 – hs – 0.4
⇒ hs = 5.5 mCorrect Option: C
σc = NPSH H ⇒ 0.144 = NPSH 25
∴ NPSH = 3.6 m
NPSH = Hatm - hv - hs - h2
Patm = Hatm = 9.8 m of water
Pv = Hv = 0.3 m of water
h2 = 0.4
⇒ 3.6 = 9.8 – 0.3 – hs – 0.4
⇒ hs = 5.5 m
- Velocity distribution in a boundary layer flow over a plate is given by (u/um) = 1.5η where, η = y / δ ; y is the distance measured normal to the plate; δ is the is the boundary layer thickness; and um is the maximum velocity at y = δ. If the shear stress t, acting on the plate is given by
τ = K( μum )/ δ
where, μ is the dynamic viscosity of the fluid, K takes the value of
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u = 1.5 η = 1.5 × y um δ ∴ u = 1.5 × y × um δ du = 1.5 × um dy δ τ = μ (1.5 × μm) δ = 1.5 (μ × μm) δ τ = k (μ.μm) δ
∴ k = 1.5Correct Option: C
u = 1.5 η = 1.5 × y um δ ∴ u = 1.5 × y × um δ du = 1.5 × um dy δ τ = μ (1.5 × μm) δ = 1.5 (μ × μm) δ τ = k (μ.μm) δ
∴ k = 1.5