Centrifugal pumps are vital components in various industries, facilitating efficient fluid handling. However, they can also be a source of operational challenges. This article answers the top 10 questions about centrifugal pumps to help you understand and optimize your pump systems.
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A centrifugal pump transfers fluid by converting rotational kinetic energy into hydrodynamic energy. Fluid enters the pump impeller along its axis, is pushed outward by the impeller’s rotation, and exits radially, gaining both speed and pressure.
Learn more about Centrifugal Pumps: Types, Applications, and Benefits
The primary types include single-stage, multi-stage, submersible, and end-suction centrifugal pumps, each suited for different applications based on flow rate, pressure requirements, and installation environment.
Selecting the right pump involves understanding your system’s flow rate, head requirement, fluid properties, and the operational environment. This ensures the pump’s specifications align with the system’s needs.
Common issues include clogging, mechanical seal failure, bearing damage, and pump cavitation, often resulting from improper operation, lack of maintenance, or unsuitable pump selection.
Cavitation can be prevented by ensuring that the pump operates within the designed conditions for NPSH (Net Positive Suction Head), reducing the fluid temperature, or increasing the pressure at the suction of the pump.
Regular maintenance, such as routine inspections, cleaning, lubrication of bearings, seal replacements, and checking for alignment and balance, are crucial for extending a pump’s life.
Troubleshooting steps include checking for blockages in the suction or discharge lines, ensuring the pump is properly primed, verifying that the impeller is not damaged or excessively worn, and ensuring that valves are open and operational.
Learn how to Select and Install a Centrifugal Pump for Your Industrial Application
Yes, but with reduced efficiency. Pumps for viscous fluids are typically designed with closer internal clearances and may operate at lower speeds to handle the increased resistance and prevent energy losses.
Improving efficiency can be achieved by matching the pump to the system requirements, minimizing pipe resistance, using speed controls like VFDs (Variable Frequency Drives) to adjust pump operation, and regularly maintaining the pump.
Priming a centrifugal pump involves filling the pump casing and the suction line with the pumped fluid to expel all air before starting the pump. Some pumps are self-priming, which automates this process.Top 5 Centrifugal Pump Maintenance Tips to Extend Lifespan
Top 5 Centrifugal Pump Maintenance Tips to Extend Lifespan
Understanding and effectively managing centrifugal pumps is crucial for maximizing efficiency and prolonging the lifespan of these essential machines. With the answers to these top questions, you can ensure more reliable and efficient pump operation in your facility.
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1. What are the centrifugal pumps?
Centrifugal pumps are the mechanical devices which pump or transport various fluids by converting their rotational kinetic energy into hydrodynamic energy.
2. Why the name centrifugal pump?
A centrifugal pump uses centrifugal force
3. Where the centrifugal pumps find applications in power plants?
Read reference books for power plant O&M
4. How do you specify the centrifugal pumps?
Centrifugal pumps are specified as bellow
5.What are the various parts of centrifugal pumps?
Centrifugal pumps have following parts
6.What are the energy conversions take place in centrifugal pumps
In centrifugal pumps hydraulic energy is being converted into kinetic energy
7.What types of reducers are used at pump suction & discharge ends?
Suction side: Eccentric type & Discharge side: Concentric
8.What are the two main types of centrifugal pumps?
Axial flow & Radial flow
9.What is the function of impeller in centrifugal pumps?
It converts kinetic energy of pump into hydrodynamic energy by rotary motion
10.What is the function of pump casing?
Casing converts velocity head from impeller into pressure head & also guides the flow to the discharge end.
11. What are the types of pump casing?
Volute & diffusers are two different types of pump casing
12. What do you mean by volute?
A volute is a spiral-like geometry with an increasing through-flow area, reducing the velocity of the fluid and increasing the static pressure
13. What are the different types of volutes?
Single volute & Double volute
15. Write down the working principle of centrifugal pumps
In centrifugal pumps, fluid enters the impeller through inlet eye & exists along the circumference between the vanes of impeller. This impeller is connected to shaft & in turn to motor, this rotary motion of the impeller converts kinetic energy of the fluid into hydrodynamic energy.
16.What are the types of impellers?
Open impeller: As its name suggests, an open impeller has vanes that are open on both sides without any protective shroud. These are structurally weak.
These are used for low flow & low head applications. Generally used for pump solids or sludge. These require much NPSH.
Semi open impeller: Semi-open impellers have a back-wall shroud that adds mechanical strength to the vanes.
Closed impeller: Are very robust & require low NPSH
Impellers are also classified as single suction & Double suction
17.What are the rotary & stationary parts of the pumps?
Rotary parts:
Stationary Parts
18.Why eccentric reducers are used at pump suction side?
To avoid air locking & cavitation eccentric reducers are used at suction side
19. What do you mean by the NPSH in pumps?
It is the net positive head required at pump suction to avoid cavitation
20. What do you understand by the term cavitation?
Cavitation is the formation & collapsing of vapor bubbles at pump’s suction
21. How the cavitation does affect the pump’s life?
22. What are the factors considered for centrifugal pumps design?
23. What are the materials used for pump casing?
Generally cast steel or cast iron are used for single stage centrifugal pumps
24. What are the materials used for Impellers?
Impellers are made up of cast iron, gun metal & stain less steel
25. What is the function of wear ring?
As the name indicates it protects the wear & tear of impeller
26. What do you mean by static suction head in pump?
Therefore, the static suction head is the vertical distance from the center line of the pump to the free level of the liquid to be pumped.
27. What do you mean by static suction head in pump?
Static discharge head is the vertical distance between the pump centerline and the point of free discharge or the surface of the liquid in the discharge tank.
28. What do you mean by total static head?
Total static head is the vertical distance between the free level of the source of supply and the point of free discharge or the free surface of the discharge liquid.
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29. What do you mean by total head?
It is total dynamic discharge head plus total dynamic suction head
Note: If source water level is below the pump center line, then
Total head = Discharge head Suction lift
If source Water level is above the pump suction line, then
Total head = Discharge head-Suction head
30. What are the problems associated with centrifugal pumps?
Following are the common problems associated with pumps
31. What are the reasons for no delivery or no discharge in centrifugal pumps?
Hydraulic Bearing Puller-5 MT
33. What are the reasons for over load of pump?
34. What are the potential reasons for pump vibrations?
35. Too much noise coming from pump inside, what does this mean?
36. What are the common mistakes done during pump installation?
37. What are the safety protections & interlocks given for a centrifugal pumps?
38. How do you increase the head & flow of pump by modifying impeller size?
By increasing the impeller diameter head & flow can be increased
By increasing the impeller width flow can be increased
39. What are the reasons for reduction of pump efficiency?
Calculation part
40. How do you calculate NPSHA?
NPSHA is Net positive suction available
NPSHA = Atmospheric pressure + static head - vapor pressure - pressure loss in the suction piping - pressure loss due to the suction strainer.
41. A centrifugal pump of rated capacity 75 M3/Hr & total head 35 meter is supplying water to fill a tank in 2 hours, calculate the total power consumption. Consider pump & motor efficiency 50% & 85% respectively
Power consumption = Pump flow in m3/sec X Pump total head in meter X fluid density X g / ( X Pump eff. X Motor eff)
Power consumption = (75/) X 35 m X kg/m3 X 9.81m/s2 / ( X 0.5 X 0.85)
Power consumption = 16.83 KWH
Power consumption in 2 hours = 16.83 X 2 = 33.66 KW
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42. A centrifugal pump having hydraulic power 22 KWH, discharge & suction head 55m & 12m respectively
Calculate the pump flow in m3/hr, assume density of water 990 kg/m3
Pump flow = Pump hydraulic power X / (Pump total head X density of fluid kg/m3 X 9.81 m/s2)
Pump flow = 22 X /( (55-12) X 990 X 9.81)
Pump flow = 0.052 m3/sec
Pump flow in M3/hr = 0.052 X = 189.6 M3/hr
43. A centrifugal pump having hydraulic power 15KWH & pump efficiency 65% calculate the pump shaft power
Pump shaft power = Pump hydraulic power / Pump efficiency = 15 / 0.65 = 23 KW
44. A centrifugal pump produces flow 20M3/hr (Q1) flow at rated speed RPM (N1) , then calculate the flow of pump at RPM(N2)
We have pump affinity law
Q1/Q2 = N1/N2
20 / Q2 = /
Q2 = 13.33 M3/hr
45. A centrifugal pump consumes power of 25KW (P1) at speed of RPM (N1), after reducing certain RPM its power consumption reduces by 5 KW (P2), calculate that speed
We have pump affinity law
P1/P2 = (N1/N2)3
25 / 5 = ( / N2)3
N2 = 877.2 RPM
46. A centrifugal pump produces 150 m (H1) head at RPM (N1), calculate the head produced if its speed reduced to 50%
We have pump affinity law
H1 / H2 = (N1/N2)2
N2 = N1 X 50% = X 0.5 = RPM
150 / H2 = ( / )2
H2 = 37.5 meter
47. A centrifugal pump having impeller diameter 250 mm produces flow 250 M3/hr, calculate the diameter of impeller to produce flow 300 M3/hr
We have
Q1 / Q2 = D1 / D2
250 / 300 = 0.250 / D2
D2 = 0.35 m = 350 mm
48. A centrifugal pump having impeller diameter 300 mm produces 250 m head & what could be the diameter if we want to reduce the head by 30m
Reduced head = 250 – 30 = 220 m
We have
H1 / H2 = (D1/D2)2
250 / 220 = (300 / D2)2
D2 = 281.4 mm
49. A centrifugal pump having impeller diameter 150 mm (D1) consumes 15 kw (P1), what is the size of impeller if we want reduce power by 4 KW
P2 = P1-4 = 15-4 = 11 KW
We have
P1 / P2 = (D1 / D2)3
15 / 11 = (150 / D2)3
D2 = 135.2mm
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