Chapter 3: Problem 3
The cavitation number is defined as \(C a=\frac{p-p_{\text {vap }}}{(1 / 2) \rho \mathrm{v}^{2}}\). Now, for ethanol produced by sugar fermentation, a company has installed a pump for the transport of the liquid product, which is assumed to be pure. The ambient pressure is \(1020 \mathrm{hPa}\) and the pump is situated \(1 \mathrm{~m}\) below a vessel from which the product is pumped through a duct of \(10 \mathrm{~cm}\) diameter with a mass flow rate of \(25 \mathrm{t} \cdot \mathrm{h}^{-1}\). The temperature at the pump suction side is \(20^{\circ} \mathrm{C}\). At this temperature, the vapor pressure is \(5.7 \times 10^{3} \mathrm{~Pa}\). The density of ethanol is 789 \(\mathrm{kg} \cdot \mathrm{m}^{-3}\). What is the background of cavitation? Does it occur in this situation? Which assumption(s) have you made? When will there be a possibility for this phenomenon to occur?
Short Answer
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Key Concepts
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