justify the importance of pump, suction head, impelling head and the total head of a pump
What is a Pump?
Introduction to Pumps and its importance.
Moving fluids plays a major role in the process of a plant. Liquid can only move on its own power, and then only from top to bottom or from a high pressure to a lower pressure system. This means that energy to the liquid must be added, to moving the liquid from a low to a higher level.
The important characteristics of a pump are the required inlet pressure, the capacity against a given total head (energy per pound due to pressure, velocity, or elevation), and the percentage efficiency for pumping a particular fluid. Pumping efficiency is much higher for mobile liquids such as water than for viscous fluids such as molasses. Since the viscosity of a liquid normally decreases as the temperature is increased, it is common industrial practice to heat very viscous liquids in order to pump them more efficiently.
Importance of suction head
The Net Positive Suction Head (NPSH) margin is a crucial factor that is commonly overlooked while selecting a pump. It is the difference between the NPSH available (NPSHa) at the pump’s inlet and the NPSH required (NPSHr) by the pump to operate without cavitation. Cavitation is the formation of bubbles at the pump inlet, followed by their sudden collapse, which can cause permanent damage. The NPSH margin value must be positive to avoid cavitation.
Pump designers use NPSH to ensure that pumps will operate without internal damage caused by cavitation under all specified operating conditions.
NPSH can be defined in two parts:
NPSH Available (NPSHA): The absolute pressure at the suction port of the pump.
NPSH Required (NPSHR): The minimum pressure required at the suction port of the pump to keep the pump from cavitating.
NPSH or Net Positive Suction Head is a very important part of a pumping system. The systems NPSHA must be higher than the pump’s NPSHR in order for proper pump performance and to eliminate the risk of cavitation, which can damage a pump in short order and shut down operations that depend on that pump.
importance of impelling head
In typical pumps used in space rocket engines, an indu-cer is employed upstream of a main centrifugal impellerin order to avoid unacceptable cavitation, improve thesuction performance, and reduce the propellant tankpressure and weight. Inducer design is focused onobtaining sufficient cavitation margin rather than highefficiency. The required net positive suctionhead (NPSH) of a centrifugal pump is reduced byemploying an inducer upstream of a centrifugal impel-ler . Pump efficiency is the ratio of the liquid horsepow-er delivered by the pump and the brake horsepow- er delivered to the pump shaft. When selecting a pump, a key concern is optimizing pumping effi-ciency. It is good practice to examine several perfor-mance charts at different speeds to see if one model satisfies the requirements more efficiently than another. Whenever possible the lowest pump speed should be selected, as this will save wear and tear on the rotating parts. The pump performance curve also gives information on pump efficiency. The efficiency curves intersect with the head-capacity curve and are labeled with percentages. The pump’s efficiency varies through-out its operating range. Each pump will have its own maximum efficiency point. The best efficiency point (BEP) is the point of highest efficiency of the pump. The impeller is subject to axial and radial forces, which get greater the further away the operating point is from the BEP. These forces manifest them-selves as vibration depending on the speed and construction of the pump. The point where the forces and vibration levels are minimal is at the BEP. Pumps should be sized as close as possible to its best efficiency point or flow rate. This not only makes the pump more efficient but also improves
Importance of the total head of a pump
justify the importance of pump, suction head, impelling head and the total head of a pump
1- Calculate the net positive suction head (NPSH) of the pump using the following data. i) - Vapor pressure of liquid -2.685 x 104 Pa i) - Distance between the level of liquid in the reservoir and suction line 1.2 m. The pump is above the liquid level. ii) -The density of liquid 865 kg/m3 iv)- Friction in the suction line 3.5 J/kg v) - Reservoir is open to atmosphere 2- Liquid octane shall be drawn from an open suction...
7.14 The pump in Fig. 7.20 delivers water from the lower to the upper reservoir at the rate of 0.057 m3/s. The energy loss between the suction pipe inlet and the pump is 1.83 m and that between the pump outlet and the upper reservoir is 3.66 m. Both pipes are 6-in Schedule 40 steel pipe. Calculate (a) the pressure at the pump inlet, (b) the pressure at the pump outlet, (c) the total head on the pump, and (d)...
02. centrifugal pump draws benzene at 25°C (sp. weight of benzene 8.59 kN/m) om a tank whose level is 2.6 m below the pump inlet. The atmospheric pressure (abs). The head loss in the suction piping due to friction and minor osses is 0.8 N.m /N. The vapor pressure of benzene is 13.3 kPa (abs). Determine he available net positive suction head (NPSH) and tell f it is acceptable or not. (10 points) Discharge ine Flew 2.6 m What is...
Q4. A pump draws water from a large reservoir and delivers it to another reservoir whose water surface is 10 m higher than the pump centreline and that the pump is 1.5 meter above the suction reservoir. The total suction and deliver pipe used is 21.1 m in length, 9 cm in diameter and has a Darcy friction factor f0.0339. The pump operates at 750 rpm and its characteristic performances are given in table below: Q (m3 s H (m)15...
A pump is located 20 feet below a supply reservoir. The head loss in the pipe from the reservoir to pump is 2.6 ft of water. Assuming atmospheric pressure to be 14.7 psia and vapor pressure of water to be 0.256 psia, the Net Positive Suction Head Available (NPSHA) is:
when a laboratory test was carried out on a pump, it was found that, for a pump total head of 36m at a discharge of 0.05cubic meters per second, cavitation began when the sum of the static pressure plus the velocity head at inlet was reduced to 3.5m. the atmospheric pressure was 750mmHg and the vapor pressure of water was 1.8kPa. if the pump is to operate at a location where atmospheric pressure is reduced to 620mmHg and the vapour...
Question (a) Sulphuric acid is flowing through a pipe (2.5 inch diameter, 50 ft length) in a velocity of 0.006 m2/s. The sulphuric acid has a viscosity of 25 mN.s/m² and density of 1680 kg/m² while the roughness of the pipe surface is 1.3 mm. If the operating temperature is 290K, determine fluid flow (i.e. laminar, turbulent or others). (Given that 1 m= 39.37 inch) (b) Define pump, suction head, impelling head and the total head of a pump. (c)...
fluid Q2: A centrifugal pump with an impeller diameter of 220 mm has to pump 0.02 mº/s of brackish water to an RO unit with following performance data at the best efficiency point: impeller speed =3000 rpm, total head= 68 m, net positive suction head=1.8 m, input power=16 hp. Evaluate the performance of a homologous pump with twice the impeller diameter operating at half the impeller speed. (15 Marks) 2016)
1.) A pump operating at 1205 rpm discharges 2360 gpm at a total head of 113 feet. If the pump speed is increased to 1380 rpm, then what is the corresponding brake horsepower (BHP) if the pump efficiency is 65%?
5.) A pump operating at 1170 rpm discharges 2000 gpm at a total head of 109 feet. If the pump speed is increased to 1300 rpm, then what is the corresponding brake horse power (HP) if the pump efficiency is 63%?