The pumping system shown below consists of a suction pipe of length 3m and diameter 80mm; delivery pipe of length 6m and diameter 80mm; 4 elbows, each with a loss coefficient of k = 0.3; total static lift = 6m; tank entry and exit loss coefficients 0.5 and 1.0, respectively; suction and delivery pipe friction factor f = 0.007Darcy. A Robuschi 150-500 pump rotates at 1470 rpm and the desired flow rate is a minimum of 200 m3/h. Complete the following tasks: 1. Draw the system curve as described above on the Roubuschi pump curve data sheet supplied. Work in increments of Q 50m3/h starting at 0 (7-point curve) 2. Would you advise the client to select the ?400 or ?460 impeller? Give two reasons for your answer. If the ?400 impeller is used: Assume: • the gauge pressure in the suction tank at 115 kPa, • the vapour pressure of the water at its average operating temperature at 20C • suction height as 1.5 m. 3. Is the pump likely to cavitate? Support answer with a NPSH calculation approach. 4. Describe two steps that could be taken to reduce the likelihood of cavitation.
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To draw the system curve, we need to calculate the total head loss for different flow rates. We can use the Darcy-Weisbach equation to calculate the frictional head loss in the pipes: hf = f * (L/D) * (V^2/2g) where hf is the frictional head loss, f is the Show more…
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Sri K.
A pump is required to deliver 240 gal/min of water at 15°C from a vented lower reservoir to a pressurized tank (see figure). The suction line is 3 m long and the discharge is 120 m. It is observed that the atmospheric pressure is 88 kPa and the vapor pressure is considered to be 2.45 kPa. Calculate the following: a) Pump Head (hA) b) Select a suitable pump from the available charts c) Calculate the NPSHA and state if the pump will run cavitation-free or not. d) If the rpm is increased by 30%, calculate the new flow rate, new head, and power required. e) The pressure at the pump outlet.
Adi S.
A pump delivers 0.045 m³/s of water through a 50-m-long suction pipe. The required net positive-suction head is NPSHᵣ = 3.96 m. The pipe's inner diameter is 0.128 m with absolute roughness such that f = 0.024 (constant). Atmospheric pressure is 99 kPa (absolute) and water properties are: vapour pressure pᵥ = 2.34 kPa (absolute), γ = 9.79 kN/m³, and ν = 1 E-6 m²/s. (a) What is the suction pipe flow velocity V (in m/s)? (b) What is the head loss hբ (in metres) in the suction pipe assuming f = 0.024? Minor losses may be ignored. (c) What should the value of NPSHₐ be at the pump inlet if cavitation is to be avoided? Include a reasonable safety factor. (d) What is the highest location of z₁ of the pump centre-line relative to the reservoir's free-surface if cavitation is to be avoided? (e) Will the pump be installed above or below the reservoir surface?
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