Abstract of the important characteristics of a centrifugal
pump that are working at constant speed and varying the discharge value
In this
experiment, there is complete information about the important characteristics
of a centrifugal pumps that are working at constant speed and varying the
discharge value. This experiment will be done through the help of closed water
circuit that contains a centrifugal pump with one motor drive and a transplant
water tank.
Aims and objectives the important
characteristics of a centrifugal pumps that are working at constant speed and
varying the discharge value
The main
aim of this experiment is to investigate important characteristics of the
centrifugal pumps that are operated at constant speed and varying the discharge
value.
Background of the study the important characteristics of a centrifugal
pumps that are working at constant speed and varying the discharge value
It can be
noted that centrifugal pumps are also known as work absorbing turbomachines.
They are mostly used for transporting fluids from one end to another. The centrifugal
force is generated by the rotation of the pump impeller. Moreover, such forces
are used for delivering water.
Description of apparatus the important
characteristics of a centrifugal pumps that are working at constant speed and varying
the discharge value
The main
apparatus for this experiment is given below
·
A
complete closed water circuit that contain centrifugal pump with a drive motor
connected with it and transplant water tank.
·
Variable
speed is given through frequency converter
·
For
observing the pump impeller there is need of a transparent housing
·
The
pressure of inlet and outlet side of the pump is adjusted by valves
·
Required
sensors for reading inlet and outlet temperature, pressure and flowrate
·
GUNT
software with required control functions
Methodology the important characteristics of a
centrifugal pumps that are working at constant speed and varying the discharge
value
The whole
circuit diagram is given by this
·
In
the first step there is need to bleed the pump demonstrator.
·
Now
after this open the valve V2 completely
·
Leave
the pump for receiving the required speed in RPM
·
Now
after this, just record the measuring values of the suction pressure P1 and
pump outlet pressure P2, the hydraulic power volume flow Q, the
electrical power, and efficiency
·
Now gradually close the valve V2 for decreasing volume and then
take measurement of the required point.
·
Now repeat the last step until the flor rate is controlled
properly
Data, results graphs the important characteristics of a centrifugal
pumps that are working at constant speed and varying the discharge value
TEST RESULTS the important characteristics of a
centrifugal pumps that are working at constant speed and varying the discharge
value
#
|
RPM
|
Q(l/sec)
|
P1(Pa)
|
P2(Pa)
|
Tem(oC)
|
Pel(W)
|
1
|
3000
|
0
|
600
|
101060
|
31.372
|
174.75
|
2
|
3000
|
0.05140
|
380
|
75940
|
31.856
|
181.88
|
3
|
3000
|
0.11125
|
260
|
80920
|
32.420
|
188.80
|
4
|
3000
|
0.17624
|
-840
|
79240
|
32.572
|
191.01
|
5
|
3000
|
0.22787
|
-1900
|
72280
|
32.6528
|
196.90
|
6
|
3000
|
0.27110
|
-2590
|
67010
|
32.783
|
199.08
|
7
|
3000
|
0.35059
|
-4440
|
54400
|
32.789
|
207.19
|
MODEL CALCULATIONS
#
|
Delta P
|
H(m)
|
P out (W)
|
Efficiency (%)
|
Dimensionless Specific speed
|
1
|
10640
|
1085.71429
|
0
|
0
|
0
|
2
|
75560
|
7710.20408
|
3883.78
|
21.4563
|
3.7E-10
|
3
|
80660
|
8230.61224
|
8973.43
|
47.729
|
4.5E-10
|
4
|
80080
|
8171.42857
|
14113.3
|
73.8916
|
5.8E-10
|
5
|
74180
|
7569.38776
|
16903.4
|
86.2379
|
8.3E-10
|
6
|
672691
|
68641.9388
|
182367
|
91.6414
|
1.2E-12
|
7
|
58840
|
6004.08163
|
20628.7
|
99.6547
|
2.1E-09
|
Maximum efficiency the important
characteristics of a centrifugal pumps that are working at constant speed and
varying the discharge value
99.6547
Discharge according to maximum efficiency
0.35059
Input power according to maximum efficiency
207.19
Head according to maximum efficiency
6004.08163
Graphs
Volume flow rate (Q) Vs manometric Head (H)
Volume
flow rate (Q) Vs Hydraulic power (Phy)
Volume flow rate (Q) Vs Electrical Power (Pel)
Volume
flow rate (Q) Vs Efficiency (h)
Interpretation and discussion of results,
including errors and how to minimize them
From all
the graphs, it can be seen that there is quite low effect of discharge of the
pump on the efficiency, hydraulic power, electrical power and also monomeric
head of the pump. Moreover, the next thing is that there is just a few value
change in the discharge of the pump and the centrifugal pump efficiency is
increased a lot. As it can be seen from the model calculation table and test
results table. There is little bit change in the value of the discharge pump
and its efficiency is almost approaches to 100 percent. This is a huge point
for the pump and its discharge value. Moreover, the efficiency is gradually increases
as the value of discharge pump is increasing.
Conclusion the important characteristics of a
centrifugal pumps that are working at constant speed and varying the discharge
value
Summing up
all the discussion from above, it is concluded that this experiment is
discussing important characteristics of centrifugal pump. As it can be seen
from the model calculation table and test results table. There is little bit
change in the value of the discharge pump and its efficiency is almost
approaches to 100 percent. In centrifugal pump, discharge of the pump and
monomeric head is extremely important characteristics.
Experiment 2
Abstract
In this
experiment, there is proper information about the performance of the
centrifugal pump. This can be done through varying the impeller size and its
speed in a proper way. This is because many pumps are operated at different
speeds. A proper experiment is performed for checking the effect if speed and
impeller size of the centrifugal pump.
Aims and objectives of the centrifugal pumps
through the help of varying the speed and impeller size of the pump
The main
aim of this experiment is to analyse the performance of the centrifugal pumps
through the help of varying the speed and impeller size of the pump.
Background of the centrifugal pumps through the
help of varying the speed and impeller size of the pump
It can be
noted that there are many centrifugal pumps that can be operated easily at
different speeds for obtaining different capacities. Moreover, another thing is
that different size of pump casing can easily accommodate impeller of different
diameters in an efficient way. The next thing is that it is extremely important
to understand the manner in which power, head, and capacity when there is
change in the speed of the pump. All of these relations are named as affinity
laws and are given below. The symbol N is referring to the rotational speed of
the impeller and it is given in revolutions per minutes. Now according the
varying speed there are some parameters and they are given by
Description of apparatus of the centrifugal
pumps through the help of varying the speed and impeller size of the pump
The main
apparatus for this experiment is given below
·
A
complete closed water circuit that contain centrifugal pump with a drive motor
connected with it and transplant water tank.
·
Variable
speed is given through frequency converter
·
For
observing the pump impeller there is need of a transparent housing
·
The
pressure of inlet and outlet side of the pump is adjusted by valves
·
Required
sensors for reading inlet and outlet temperature, pressure and flowrate
·
GUNT
software with required control functions
Methodology of the centrifugal pumps through
the help of varying the speed and impeller size of the pump
·
Set
the apparatus according to the given information
·
Follow
all regular steps from the experiment 1
·
Now
change the value of discharge of the pump and impeller size
·
Now
record the values in the given table and analyse the results
Data, results and graphs of the centrifugal pumps through the help of
varying the speed and impeller size of the pump
TEST
RESULTS
Use the same test result obtained in experiment
1 for fully opened valve
#
|
RPM
|
Q(l/sec)
|
P1(Pa)
|
P2(Pa)
|
Tem(oC)
|
Pel(W)
|
1
|
3000
|
0
|
600
|
101060
|
31.372
|
174.75
|
2
|
3000
|
0.05140
|
380
|
75940
|
31.856
|
181.88
|
3
|
3000
|
0.11125
|
260
|
80920
|
32.420
|
188.80
|
4
|
3000
|
0.17624
|
-840
|
79240
|
32.572
|
191.01
|
5
|
3000
|
0.22787
|
-1900
|
72280
|
32.6528
|
196.90
|
6
|
3000
|
0.27110
|
-2590
|
67010
|
32.783
|
199.08
|
7
|
3000
|
0.35059
|
-4440
|
54400
|
32.789
|
207.19
|
#
|
Delta P
|
H(m)
|
P out (W)
|
Efficiency(%)
|
Dimensionless Specific speed
|
1
|
10640
|
1085.71429
|
0
|
0
|
0
|
2
|
75560
|
7710.20408
|
3883.78
|
21.4563
|
3.7E-10
|
3
|
80660
|
8230.61224
|
8973.43
|
47.729
|
4.5E-10
|
4
|
80080
|
8171.42857
|
14113.3
|
73.8916
|
5.8E-10
|
5
|
74180
|
7569.38776
|
16903.4
|
86.2379
|
8.3E-10
|
6
|
672691
|
68641.9388
|
182367
|
91.6414
|
1.2E-12
|
7
|
58840
|
6004.08163
|
20628.7
|
99.6547
|
2.1E-09
|
Choose 4 different rotational speed
Choose
four different impeller diameters
rotational
speed
|
impeller
diameter
|
Q
|
H
|
Power
|
22
|
17
|
0.048544
|
1113287.98
|
55327573146
|
23
|
18
|
0.105395
|
56318444.5
|
6.84532E+11
|
24
|
19
|
0.167428
|
64355829
|
2.6706E+12
|
25
|
20
|
0.216477
|
63433632.7
|
4.58823E+12
|
Interpretation and discussion of results of the centrifugal pumps through the help of
varying the speed and impeller size of the pump
According to
the given theory it can be noted that the capacity of the impeller is
completely directly proportional to the speed of the pump. Moreover, head of
the pump is directly proportional to the square of the speed of the pump. It is
also same for the diameters of the impeller also. From the results it can be
noted that as the rotational speed of the pump increased its capacity is also
increased with it.
Conclusion of the centrifugal pumps through the
help of varying the speed and impeller size of the pump
Summing up
all the discussion from above, it is concluded that centrifugal pumps also
contains varying speed and impeller diameters. Moreover, another thing is that
different size of pump casing can easily accommodate impeller of different
diameters in an efficient way. From the results it can be noted that as the
rotational speed of the pump increased its capacity is also increased with it. It
shows that the performance of the centrifugal pumps is dependent on the
rotational speed and also the impeller diameter of the pump.
Experiment 3
Abstract
In this
experiment, there is complete information about the performance of centrifugal
pumps in series and parallel. This experiment will deal with information
related to these pumps and how their behaviour is changed when they are
operated parallel or in series. It will also show how the performance of such
pumps is effected through such modifications
Aims and objectives
The main
aim of this experiment is to analyse the performance of the centrifugal pumps
when they are connected in series and parallel.
Background
According
to the given information about the pumps, it shows that a single pumps is not
enough for producing such performance according to requirement. If these pumps
are combined then due to this performance is increased of the pump system.
Series connection of pumps
This shows
that if the system pressure head is extremely high for the pump then multistage
pump is used. In this several pumps are attached in series. Now the fact is
that if two pumps are connected with each other in series in a pipeline then
new characteristic curve is obtained. This can be done by adding the pressure
head of the different pumps for certain flow rate. But the main thing is that
flow rate of the pump is completely same. This shows that the total pressure of
the two pumps is given by
But the
flow rate of these pumps are completely same
Pumps attached in parallel
It can be
noted that when these two pumps are operated in parallel then the total head of
these pumps will be completely same. On the other hand, its flow rate is
increased. Moreover, its head capacity curve is obtained through adding the
flow rates of the single pump curve at the same time. The flow rate of the pump
is achieved by adding them together
On the
other hand, total head value is completely same
Description of apparatus
The main
apparatus for this experiment is given below
·
A
complete closed water circuit that contain centrifugal pump with a drive motor
connected with it and transplant water tank.
·
Variable
speed is given through frequency converter
·
For
observing the pump impeller there is need of a transparent housing
·
The
pressure of inlet and outlet side of the pump is adjusted by valves
·
Required
sensors for reading inlet and outlet temperature, pressure and flowrate
·
GUNT
software with required control functions
Methodology
·
Repeat
all steps from the first experiment
·
Now
attach the pumps in series and check its performance
·
Record
the reading of head and flow of the pumps connected in series
·
Now
attach the pumps in parallel and check its performance
·
Record
the reading of head and flow of the pumps connected in parallel
Data, results and graphs
#
|
RPM
|
Q(l/sec)
|
P1(Pa)
|
P2(Pa)
|
Tem(oC)
|
Pel(W)
|
1
|
3000
|
0
|
600
|
101060
|
31.372
|
174.75
|
2
|
3000
|
0.05140
|
380
|
75940
|
31.856
|
181.88
|
3
|
3000
|
0.11125
|
260
|
80920
|
32.420
|
188.80
|
4
|
3000
|
0.17624
|
-840
|
79240
|
32.572
|
191.01
|
5
|
3000
|
0.22787
|
-1900
|
72280
|
32.6528
|
196.90
|
6
|
3000
|
0.27110
|
-2590
|
67010
|
32.783
|
199.08
|
7
|
3000
|
0.35059
|
-4440
|
54400
|
32.789
|
207.19
|
Two pumps are connected in parallel
Head of second pump is 1085.71429
#
|
Delta P
|
H(m)
|
P out
(W)
|
Efficiency(%)
|
Dimensionless
Specific speed
|
1
|
10640
|
2171.42429
|
0
|
0
|
0
|
2
|
75560
|
7710.20408
|
3883.78
|
21.4563
|
3.7E-10
|
3
|
80660
|
8230.61224
|
8973.43
|
47.729
|
4.5E-10
|
4
|
80080
|
8171.42857
|
14113.3
|
73.8916
|
5.8E-10
|
5
|
74180
|
7569.38776
|
16903.4
|
86.2379
|
8.3E-10
|
6
|
672691
|
68641.9388
|
182367
|
91.6414
|
1.2E-12
|
7
|
58840
|
6004.08163
|
20628.7
|
99.6547
|
2.1E-09
|
Pumps connected in parallel
#
|
RPM
|
Q in parallel
|
P1(Pa)
|
P2(Pa)
|
Tem(oC)
|
Pel(W)
|
1
|
3000
|
0.435
|
600
|
101060
|
31.372
|
17400.75
|
2
|
3000
|
0.4864
|
380
|
75940
|
31.856
|
18100.88
|
3
|
3000
|
0.54625
|
260
|
80920
|
32.42
|
18800.8
|
4
|
3000
|
0.61124
|
-840
|
79240
|
32.572
|
19100.01
|
5
|
3000
|
0.66287
|
-1900
|
72280
|
32.6528
|
19600.9
|
6
|
3000
|
0.7061
|
-2590
|
67010
|
32.783
|
199000.1
|
7
|
3000
|
0.78559
|
-4440
|
54400
|
32.789
|
20700.19
|
Graphs
Interpretation and discussion of results
From the
above graph it is concluded that there is no change in the value of flow rate
of the pumps when they are connected in series. On the other hand, it can be
noted that there is also no change in the head when the pumps are connected in
parallel. For analysing, the head for second pump is selected as 1085.72. The
next thing is that for parallel pump flow rate of second pump is given by
0.435.
Conclusion
Summing up
all the discussion from above, it is concluded that this experiment discusses
series and parallel performance of the centrifugal pumps. For analysing, the
head for second pump is selected as 1085.72. The next thing is that for
parallel pump flow rate of second pump is given by 0.435. The graphs are
presented and shows the proper results that there is no change in the flow rate
when they are attached in series and also there is no change in the head when
they are connected in parallel.
Experiment 4
Abstract
In this
experiment, there is complete information about the operating points of the
centrifugal pumps. It can be noted that there are about three important
characteristics of the pump are flow rate, head and its efficiency. This
experiment will cover these points properly.
Aims and objectives
The main
aim of this experiment is to analyse the operating points of the centrifugal
pumps.
Background
it can be
noted that the characteristic curve of the pump is only plotted through the
test results. Moreover, this shows that if a pump is connected to a water
piping system then its system head is given by this
Description of apparatus
The main
apparatus for this experiment is given below
·
A
complete closed water circuit that contain centrifugal pump with a drive motor
connected with it and transplant water tank.
·
Variable
speed is given through frequency converter
·
For
observing the pump impeller there is need of a transparent housing
·
The
pressure of inlet and outlet side of the pump is adjusted by valves
·
Required
sensors for reading inlet and outlet temperature, pressure and flowrate
·
GUNT
software with required control functions
Methodology
·
Repeat
the same procedure for the experiment one
·
Now
measure the head and record it
·
Measure
the flow rate of the pump and record it
·
Check
the efficiency of the pump
·
Calculate
the system head of the pump and record it.
Data, results and graphs
Q
|
H (m)
|
Eff (%)
|
Hsy(m)
|
0
|
22.5
|
0
|
16.5
|
0.01
|
21
|
66
|
17.655
|
0.02
|
18
|
81
|
21.12
|
0.03
|
12.5
|
70
|
26.895
|
0.04
|
3
|
20
|
34.98
|
Interpretation and discussion of results
From the
above graphs it can be noted that as the efficiency of the pumps is increases
in the start as the flow rate is gradually increases but it declines after the
certain point. On the other hand, head of the system is exponentially
increasing with respect to flow rate of the pump. In the last, the value of
head is decreases as the flow rate is increased. This shows that flow rate and
head of the pump is showing inverse relationship.
Conclusion of the centrifugal pumps through the
help of varying the speed and impeller size of the pump
Summing up
all the discussion from above, it is concluded that this experiment is
discussing some important characteristics of the pump. As the results are
showing such behaviour in the given graphs. The efficiency of the pumps is
increases in the start as the flow rate is gradually increases but it declines
after the certain point. The head of the system is exponentially increasing with respect to flow rate
of the pump. The value of head is decreases as the flow rate is increased.