Chapter 7: Problem 59
A model hydrofoil is to be tested. Is it practical to satisfy both the Reynolds number and the Froude number for the hydrofoil when it is operating near the water surface? Support: your decision.
Chapter 7: Problem 59
A model hydrofoil is to be tested. Is it practical to satisfy both the Reynolds number and the Froude number for the hydrofoil when it is operating near the water surface? Support: your decision.
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Get started for freeA screw propeller has the following relevant dimensional parameters: axial thrust, \(F\), propeller diameter, \(D\), fluid kinematic viscosity, \(v,\) fluid density, \(\rho,\) gravitational acceleration, \(g,\) advance velocity, \(V,\) and rotational speed, \(N .\) Find appropriate dimensionless parameters to present the test data.
By inspection, arrange the following dimensional parameters into dimensionless parameters: (a) kinematic viscosity, \(v,\) length, \(\ell,\) and time, \(t ;\) and (b) volume flow rate, \(Q,\) pump diameter, \(D,\) and pump impeller rotation speed, \(N\)
At a sudden contraction in a pipe the diameter changes from \(D_{1}\) to \(D_{2} .\) The pressure drop, \(\Delta p,\) which develops across the contraction is a function of \(D_{1}\) and \(D_{2},\) as well as the velocity, \(V\), in the larger pipe, and the fluid density, \(\rho,\) and viscosity, \(\mu .\) Use \(D_{1}, V,\) and \(\mu\) as repeating variables to determine a suitable set of dimensionless parameters. Why would it be incorrect to include the velocity in the smaller pipe as an additional variable?
A mixing basin in a sewage filtration plant is stirred by a mechanical agitator with a power input \(\dot{W} \doteq F \cdot L / T\). Other parameters describing the performance of the mixing process are the fluid absolute viscosity \(\mu \doteq F \cdot T / L^{2},\) the basin volume \(V \doteq L^{3}\) and the velocity gradient \(G \doteq 1 / T\). Determine the form of the dimensionless relationship.
An equation used to evaluate vacuum filtration is $$Q=\frac{\Delta p A^{2}}{\alpha\left(V R w+A R_{f}\right)}$$ Where \(Q \doteq L^{3} / T\) is the filtrate volume flow rate, \(\Delta p \doteq F / L^{2}\) the vacuum pressure differential, \(A \doteq L^{2}\) the filter area, \(\alpha\) the filtrate "viscosity," \(V \doteq L^{3}\) the filtrate volume, \(R \doteq L / F\) the sludge specific resistance, \(w \doteq F / L^{3}\) the weight of dry sludge per unit volume of filtrate, and \(R_{f}\) the specific resistance of the filter medium. What are the dimensions of \(R_{f}\) and and \(\alpha ?\)
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