Question

In: Mechanical Engineering

The following design and operating data were taken for a large industrial centrifugal water pump: Parameter...

The following design and operating data were taken for a large industrial centrifugal water pump:

Parameter Design Operating
Flow Q (m^3/h) 800 550
Head H (m) 55 24 (after delivery valve)
Power P (kW) 160 124
RPM 1485 1485

Required water flow rate varies from 500 m3/h to 700 m3/h. For the pump to deliver 550 m3/h, the flowrate has been reduced by partially closing the delivery valve. Motor efficiency is 93%.

a. Calculate the pump operating efficiency (the ratio of pumping power to operating pump input power delivered TO THE MOTOR.

b. Pump operating efficiency is low because of the partial valve closing to control the flowrate. What would be the best way to improve pump operating efficiency?

c. The ratio of two pump volumetric flowrates would be equal to the ratio of two pump shaft speeds to what power? The ratio of two pump operating heads would be equal to the ratio of two pump shaft speeds to what power? The ratio of two pump operating powers would be equal to the ratio of two pump shaft speeds to what power?

d. Suppose the pump energy improvement idea suggested in part b. was used for the pump. From the relations in part c., calculate the pump speed required to give a volumetric flowrate 550 m3/h. That is, (550 m3/h / design flowrate) = (RPM to deliver 550 m3/h / design RPM). From this, calculate the pumping power needed to deliver 550 m3/h using the design pumping power ratio. The difference in the operating values of the pumping power (124 kW and the pumping power with the new energy efficiency feature) is the energy savings.

Solutions

Expert Solution

(a)

power input to pump = power input to motor * efficiency of motor

= 124 * 0.93

= 115.32 kW

Pump operating efficiency = (density * Q * g * H / pump input power ) operating point * 100

= {1000 * (550/3600) * 9.81 * 24 / (115.32*1000)}* 100

= 31.19 %

.................................................................................................................................................................

(b)

In this case the speed of pump is constant ( design and operational speed are same). The best way to improve the pump efficiency is by changing its roational speed. it can be achived by utilising variable speed pump.

..................................................................................................................................................................

(c)

(Q / D3N ) pump1 =  (Q / D3N ) pump2

therefore volumetric flowrates (Q) is proportional (1st power) to pump shaft speeds (N).

(H / D2N2 ) pump1 =  (H / D2N2) pump2  

therefore pump operating heads (H) is proportional to square (2nd power) of pump shaft speeds(N).

(P / D5N3 ) pump1 =  (P / D5N3) pump2  

therefore pump operating powers (p) is proportional to cube (3rd power) of pump shaft speeds(N).

..................................................................................................................................................................

(d)

Here the pump is same thefore: D = constant

(Q1 / N1 ) =  (Q2 / N2 )

800 / 1485 = 550 / N2

N2 = 1021 RPM = new operating speed for variable speed pump

(P1 / N13 )  =  (P2 / N23)

160 / 14853 = P2 / 10213

P2 = 52 kW = power consumed in variable speed pump

The difference in the operating values of the pumping power (Energy saving) = 124 - 52 = 72 kW


Related Solutions

A centrifugal pump is to be used to pump water from a lake to a storage...
A centrifugal pump is to be used to pump water from a lake to a storage tank which is 165 feet above the surface of the lake. The pumping rate is to be 10 - 35 gal/min at a water temperature of 43°F. The water is used for drinking but will have to undergo filtration and chlorine treatment because there is sediment in the lake. The pump on hand can develop a discharge pressure of 60.0 psig pumping at a...
A model centrifugal pump with impeller diameter 365 mm is tested at its design operating condition....
A model centrifugal pump with impeller diameter 365 mm is tested at its design operating condition. The test gives the following data when pumping water, speed = 870 rev/min head = 18.9 m capacity = 73.7 L/s efficiency = 89%. A geometrically similar pump is to be designed to pump a fluid with relative density 0.78 against a head of 85 m with a flow of 450 L/s. Determine: A) The impeller size? B) The speed? C) The power input...
Design a chain drive for a Centrifugal Pump to be driven by a Steam Turbine. The...
Design a chain drive for a Centrifugal Pump to be driven by a Steam Turbine. The input speed will be 1100 RPM, and the desired output speed is 350 RPM. The conveyor requires 20.0 hp. What type of lubrication will be needed?
A centrifugal pump with an impeller diameter of 30cm and speed 1800RPM operating at its best...
A centrifugal pump with an impeller diameter of 30cm and speed 1800RPM operating at its best effiecieny point develops a head of 30m and a flow of 3900L/min. while requiring power of 24kW. This pump is scaled up to provide a flow of 11000L/min. and a head of 75m. Determine the impeller diameter, speed, and a brake power of the new pump.
1. A centrifugal water pump impeller is given an inlet and exit radius of 400 mm...
1. A centrifugal water pump impeller is given an inlet and exit radius of 400 mm and 1200 mm, and an inlet and exit blade thickness of 120 mm and 80 mm. The entering and exiting blade angles are 40o and 60o respectively. If the pump rotational speed is 575 rpm with and efficiency of 85%, determine: a) Ideal head (m) b) Fluid power for max pressure (kW) c) Shaft torque for max pressure (Nm) solutions a) 488 m b)...
A centrifugal pump lifts water against a head of 36m, the manometric efficiency being 80%. The...
A centrifugal pump lifts water against a head of 36m, the manometric efficiency being 80%. The suction and delivery pipes are both 150mm bore, the impeller is of 375mm and 25mm wide at the outlet; its exit blade angle is 250 and the specific rotational speed is 1320 rev/min. If the total loss by friction in the pipeline at this speed is estimated at 9m, calculate the probable rate of discharge at this speed.
When a centrifugal pump runs at 1500 rpm, it discharges 0.05 m3 / h of water....
When a centrifugal pump runs at 1500 rpm, it discharges 0.05 m3 / h of water. The entrance and exit radii of the rotor are given as 0.05 m and 0.15 m respectively, the wing thickness at the entrance is 0.03 m, and the wing thickness at the exit is 0.01 m. The inlet and outlet vane angles are 60o and 45o respectively, and the pump mechanical efficiency is 0.85. In this case; a) What should be the theoretical head...
A centrifugal pump delivers water at rate of 0.22 m3/s from a reservoir at a ground...
A centrifugal pump delivers water at rate of 0.22 m3/s from a reservoir at a ground level to another reservoir to height 'h' through a vertical pipe of 0.2 m diameter. Both are open to atmosphere. Power input to pump is 90 kW and it operates with 75% efficiency . f=0.004 use g=9.8 m/s2 density=1000kg/m3. Find 'h'.
Consider a centrifugal water pump whose geometry and flow conditions are as follows: Impeller outlet radius...
Consider a centrifugal water pump whose geometry and flow conditions are as follows: Impeller outlet radius – 2.5 cm, impeller inlet radius – 1.8 cm, impeller outlet width – 1 cm, design speed – 1800 rpm, Design flow rate120 liters/min, Backward-curved vanes (outlet blade angles) – 60 deg. Assuming 100% efficiency, find: a) the total head, b) absolute and relative discharge velocities, c) theoretical power required at design flow rate and d) the theoretical pump curve
A centrifugal pump has the following characteristic: outer diameter of impeller 800 mm, width of impeller...
A centrifugal pump has the following characteristic: outer diameter of impeller 800 mm, width of impeller vanes at outlet 100 mm, angle of impeller vanes at outlet 40 o . The impeller runs at 550 rpm and delivers 0.98 m 3 /s of water under an effective head of 35 m. A 500 kW motor is used to drive the pump. Determine the manometric, mechanical and overall efficiencies of the pump. Assume water enters the impeller vanes radially at inlet....
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT