Ans a) We know, System curve equation can be given as :
Hp = Z + H
where, Z = Static head = 20 m
H = head loss
=> Hp = 20 + H
At flow rate = 20 L/s or 0.02 /s.
Hp = 20 + 1() = 20 m
At flow rate = 40 L/s or 0.04 /s.
Hp = 20 + 4() = 20 m
Similarly we can calcultate head for all flow rates. Final results areshown in table below:
Q (Lit/s) | Hp (m) |
0 | 20 |
20 | 20 |
40 | 20 |
60 | 20.036 |
80 | 20.13 |
Plot the given system curve and performance curve as shown below :
The point of intersection of performance curve and system curve is operating point or duty point.Hence,
Operating flow rate corresponding to duty point = 55 L/s or 0.055 s
Operating efficiency corresponding to opearting point () = 50%
We know,
Power consumption (P) = g Q Hp /
where, Hp = Operating head corresponding to operating point = 20 m
Putting values,
=> P = 1000 x 9.81 x 0.055 x 20 / 0.50
=> P = 21.58 kW
Ans b) We know, when two similar pumps are conneted in series, the resulting performance head will be twice of head of individual pumps but flow rate remain same. Hence, performance curve for pumps in series is as follows :
Q (Lit/s) | Hp (m) |
0 | 50 + 50 = 100 |
20 | 45 + 45 = 90 |
40 | 33 + 33 = 66 |
50 | 25 + 25 = 50 |
60 | 14 + 14 = 28 |
Plot the given system curve and new performance curve as shown below
The point of intersection of performance curve and system curve is operating point or duty point.Hence,
Operating flow rate corresponding to duty point = 63 L/s
Hence, Maximum flow rate of proposed system is 63 L/s
Ans c) Now, for proposed system,
Q = 63 L/s or 0.063 /s
Hp = 20 m
Efficiency () corresponding to flow rate 63 L/s is approximate to 36%
Power consumption (P) = g Q Hp /
=> P = 1000 x 9.81 x 0.063 x 20 / 0.36
=> P = 34.34 kW
Since, power consumption of system increases significantly (from 21.58 kW to 34.34 kW) but the increase in flow rate is small (from 55 L/s to 63 L/s), the proposed system is not suitable as the efficiency of system is very low.
please give upvote if you understood the answer
thank you
A water pump has been operating at a pump station at speed 1000 rpm. The pipeline...
Problem 4 (10 points) A pipeline with two pumps (Pump A and Pump B) in series delivers water between two tanks with a total static head of 50 ft. The pipeline is 8 inches in diameter and 5000 ft in length, with a Darcy- Weisbach friction factor f = 0.025. The total minor head loss coefficient Ek 20. The characteristics of the two pumps are shown in the following table. Determine (a) the operating conditions of head and discharge, (b)...
When a water pump was tested at a rotation rate of 1500 rpm, the following data was obtained: Q (I/s) 0 10 20 30 40 50 H(m) 10.0 10.5 10.0 8.5 6.0 2.5 n (%) 0 0.40 0.64 0.72 0.64 0.40 It is proposed to use this pump to draw water from an open well and deliver it to a tank 5.5 m above. The delivery pipe is 20.0 m long and 100 mm diameter, and has a friction factor...
A 1/4-scale model centrifugal pump is tested to pump water with density of 1000 kg/m under a head of 7.5 m at speed of 500 rpm. It was found that 7.5 kW was needed to drive the model. Assuming the pumps is geometrical similar and similar mechanical efficiency, determine; (i) speed and power required by the prototype when pumping against a head of 44 m; ratio of the discharges between model and prototype; and head, capacity and power coefficient of...
Mechanical Lab II. Please answer asap with clear work. Thank you! 1. A centrifugal pump performance data are shown in the following table for water. Pump speed-2500 RPM Pa or P2 (bar) P. or Pi (bar) Volume of water(L Time (sec) Input-Power (W) -0.3 20 60 100 For this data set, calculate the following i. Pump discharge capacity Q (LUs and GPM) ii. Pump head H (m and ft) iii. Fluid power Pr (Watt) iv. Brake power Pb (Watt) v....
4) If a 60kW pump is operating at 1200 RPM, and has a Head of 250 ft, and an 8 impeller, what happens to the Head, Power, and speed if the impeller is increased by 50%? 4) If a 60kW pump is operating at 1200 RPM, and has a Head of 250 ft, and an 8 impeller, what happens to the Head, Power, and speed if the impeller is increased by 50%?
A centrifugal pump operating at 1200 rpm is delivering 10 m^3/h of water at 10 bars and requires 6 kW of shaft power at the best efficiency point. a. Determine the effiecincy of the pump b. Deterine the flow rate, discharge pressire, and required shaft power at the corresponding point of 1800 rpm. 4. A centrifugal pump operating at 1200 rpm is delivering 18 m2/h of water at 10 bars and requires 6 kW of shaft power at the best...
3. A centrifugal pump performance data are shown in the following table for water. Pump speed 2500 RPM Pe or P2 (bar) P or Pi (bar) Volume of water (L) Time (sec) Input-Power (W -0.3 20 60 100 For this data set, calculate the following: i. Pump discharge capacity Q (L/s and GPM) ii. Pump head H (m and f) iii. Fluid power Pr(Watt) iv. Brake power Pb (Watt) v. Pump overall efficiency η (%) vi. Flow rate coefficient Ca...
2. The characteristics of a 0.7 m diameter centrifugal pump impeller running at 750 rpm are as follows: 2 (m*/min) H (m) 4(%) 0 7 4 2 28 354 49 56 40 40.6 40.4 39.3 38.0 33.6 25.6 145 0 0 460 74 83 83 51 0 (a) f the pump is initially used to transfer water from one reservoir to another at the same level, determine the pump operating point if the head lost to frictional and other resistances...
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%?
(100 points) Water at 25°C is pumped at a rate of 0.075m'/s from a reservoir 20m above a pump to a free discharge (this means discharged to atmosphere) 35m above the pump. The pressure on the intake side of the pump is 150kPa and the pressure on the discharge side of the pump is 450kPa. The pipe between the reservoir and the pump is 3 meters of 5in diameter cast iron. From the pump to the discharge the pipe is...