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Laboratory Report on

Laboratory Report on

 Axial Flow Pump Test

 Axial Flow Pump Test

By

By

Walson Onyemobi

Walson Onyemobi

Student No: 08836256

Student No: 08836256

Module: CN225, Hydraulics

Module: CN225, Hydraulics

Course: MEng, Civil Engineering, Level 2

Course: MEng, Civil Engineering, Level 2

Date of Experiment: 7th March 2011

Date of Experiment: 7th March 2011

Submission Deadline: 20th March 2011

Submission Deadline: 20th March 2011

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Table of Contents:

1 INTRODUTION ... 3

2 MATERIALS AND METHOD ... 4

2.1 Method ... 4

3 THEORY AND RESULTS ... 5

3.1 Theoretical Analysis ... 5 3.2 Analysis of Results ... 6 4 SOURCES OF ERROR ... 11 5 CONCLUSION ... 12 6 REFERENCES ... 12

Table of Figures:

Figure 1: Graph of Hm (m) Against Q (m3/s) ... 9

Figure 2: Graph of Efficiency (%) Vs Discharge (m3/s) ... 9

Figure 3: Graph of PH (Joules) against Q (m3/s) ... 9

Figure 4: Graph of H1200 (Joules) against Q1200 (m3/s) ... 11

Figure 5: Graph of Q (m3/s) against P1200 (joules) ... 11

Table of Tables

Table 1: Table 1: Details of the Experimental Values Obtained For Different Pump Speeds...6

Table 2: Total Head at N = 1200rpm...7

Table 3: Total Head at N = 1300rpm...7

Table 4: Total Head at N = 1400rpm...7

Table 3: Discharge Values across the Pipe for the Three Different Pump Speeds....8

Table 4: Values of PH, PE, and η for each of the Three Pump Speed...9

Table 5: values of head, discharge, and hydraulic power under a 1200rpm base speed...11

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1 INTRODUTION

The concept of axial flow pump with respect to its performance, uses and industrial applications as opposed to centrifugal pump is quit enormous. Due to the fact that axial machines have more limited suction capacity than centrifugal pumps [3], it therefore follows that the flow generated around the section of axial machine blade becomes very sensitive to low pressure. Hence, a low intake of pressure in an axial flow pump results to flow separation and consequent loss of energy. In order to determine the flow of fluid in an axial pump which is dependent on the fluid pressure, electrical power, head across the pump etc an characteristics performance curves will be constructed,thus,the aim of the experiment; to construct the characteristics curves for an axial flow pump test.

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2 MATERIALS AND METHOD

The following materials were provided for use in the experiment.

1. 415 volts of an AC motor with a maximum speed of 1400rpm 2. Motor speedometer, measured in rev/min

3. Current meter (Amps) consumed by the motor.

4. Sets of manometers and a dall tube: used to measure pressure (in mm Hg) and the discharge (Q) through the pipe respectively.

5. Measuring tape – used to measure the downstream distances (Z1 and Z2).

2.1 Method

The following steps were carried out during the experiment.

Step 1 – the downstream and upstream distances (Z1 and Z2) were measured and recorded.

Step 2  – the valves connected from the manometers to the main pipe were fully closed. The gate valve fully opened.

Step 3 – the pump was started with an increased sped of 1100rpm and the valves opened with the gate valve now closed.

Step 4  – after reading manometer #2, the gate valve was now fully reopened and adjusted so that manometer #2 is reduced by ~ 10mm.

Step 5 – the pump control was adjusted to maintain a constant speed of 1200rpm. Step 6 – the current meter and manometers readings were measured and recorded. Step 7 – the experiment was repeated from step 4 for two different pump speeds (N = 1300 & 1400 rpm’s).Table 1 shows the experimental data obtained.

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3 THEORY AND RESULTS 3.1 Theoretical Analysis

 An axial flow pump is a type of pump that consists of a propeller, which in some instances can be driven directly by a sealed motor in a pipe (as in the case of CN225 lab) or mounted to the pipe from the outside or by a right-angle drive shaft that pierces the pipe. Axial pump always follow an axial type of flow (i.e. the flow is longitudinal) thereby producing the smallest dimensions in comparison to other pump types. This small dimensions results to the development of low head and steeply descending efficiency curve as illustrated in figure 2.

In other to determine the efficiency of the pump, the power output (hydraulic power  PH) and input (electrical power PE) needs to be evaluated. The efficiency (n) of the pump is given by the relation;

   



Where PH (hydraulic power) =



(in Joules), and PE (electrical power) = Amps × Volts in watts.

The discharge (Q) is given by

 

 



⁄ 

Where

 

are the manometer readings (in mm).

The total hydraulic head (Hm) across the pump can be calculated knowing the pressure upstream and downstream of the pump. The relationship that governs the total head is expressed below;

 

 

  



(



 



)

Using the information above, the characteristics performance curve for the axial flow pump can be constructed. A base speed of 1200rpm is used to construct the graph of the relations in equations 4,5 and 6.This is to compare the results when the pump is operating at different speeds.



 

 

⁄ 





  

⁄ 





 

 

⁄ 



Given equations 1,2 and 3 above, the relationships between the total head (HM),Hydraulic power (PH),efficiency (η) and the discharge (Q) can be established graphically, with an iso-efficiency line drown on the HM-Q graph showing how efficient or the level of performance of the axial flow.N is the pump operating speeds. Details of the calculations and graphs are given in the ‘results analysis’ section of  this report (page 5).

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3.2 Analysis of Results

Given that the total head (Hm) across the pump is related to the pressure supplied across the pipe and the manometers by the equation 3, page 4, where Z1 and Z2 are the downstream distances, Rright and Rleft are the two manometer readings at a given pump speed (N).Rho (

and



) are densities of water and mercury respectively given as 1000kg/m3& 13600kg/m3.

Table 1, below gives the experimental values obtained in the lab. Z1 = 1.46m Z2 = 1.58m R0= 9mm Reading Current  meter(Amps) Manometer #1 (m) Manometer #2 (Ri)in mm. Rleft  Rright  Pump Speed 1200rpm 1 16 0.34 0.26 155 2 17 0.32 0.28 140 3 18 0.31 0.29 125 4 18.5 0.30 0.30 110 5 19 0.29 0.31 95 6 18 0.27 0.34 80 7 17 0.26 0.34 65 8 17.5 0.26 0.34 50 9 17 0.26 0.34 35 10 18 0.24 0.36 20 11 29.5 0.11 0.48 10 Pump Speed 1300rpm 1 16.5 0.36 0.235 210 2 17.5 0.35 0.25 190 3 18.5 0.29 0.28 170 4 19 0.26 0.31 150 5 20 0.25 0.34 130 6 21.5 0.24 0.35 110 7 22 0.24 0.36 90 8 21 0.24 0.36 70 9 19.5 0.22 0.38 50 10 21 0.22 0.48 30 11 28 0.11 0.08 10 Pump Speed 1400rpm 1 18.5 0.36 0.24 240 2 21 0.33 0.27 216 3 22 0.30 0.29 192 4 24 0.25 0.34 168 5 24.5 0.24 0.35 144 6 25 0.32 0.37 120 7 24.5 0.22 0.38 98 8 23.5 0.22 0.39 72

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9 23 0.21 0.43 48

10 27 0.16 0.54 24

11 30 0.05 0.05 10

Table 6: Details of the Experimental Values Obtained For Different Pump Speeds From equation 3 above, the total head (Hm) across the pump for each manometer  readings (Rright & Rleft) and at different pump speeds is calculated below (table 2); Thus; for pump speed of 1200rpm, substituting relevant values in the equation,

Hm =

   





    

.

Therefore, following the calculations above, different Hm’s can be obtained for each N and at different manometer readings.Z1, Z2,

and



are all constant throughout.

Pump Speed (N) = 1200rpm

Reading 1 2 3 4 5 6 7 8 9 10 11 Hm(m) 2.032 2.536 2.788 3.04 3.292 3.922 4.048 4.048 4.048 4.552 7.702

Table 7: Total Head at N = 1200rpm.

Table 8: Total Head at N = 1300rpm

Pump Speed (N) = 1400rpm

Reading 1 2 3 4 5 6 7 8 9 10 11 Hm(m) 1.528 2.284 2.914 4.174 4.426 3.670 5.056 5.182 5.308 6.442 9.214

Table 9: Total Head at N = 1400rpm

Tables 2, 3 & 4 above shows the total heads across the pump at different pump operating speeds. This implies that as the pump operates (delivers fluid) at a constant speeds of 1200,1300 & 1400rpm’s there is an increase in the total head across the pump, thereby resulting to a loss in the hydraulic energy.

From equation 2 above, the discharge across the pump for each pump speed can be computed.

 

 



⁄ 

. Where Ri and R0 are the manometer #2 readings and its initial reading respectively .e.g.

 √     

⁄ 

Pump Speed (N) = 1300rpm

Reading 1 2 3 4 5 6 7 8 9 10 11 Hm(m) 1.465 1.780 2.914 3.670 4.174 4.426 4.552 4.552 5.056 6.316 7.450

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Pump Speed (N) = 1200rpm Reading 1 2 3 4 5 6 7 8 9 10 11 Q (m3/s) 0.160 0.1512 0.1 43 0.13 3 0.12 3 0.11 2 0.09 9 0.08 48 0.06 76 0.04 39 0.01325 Pump Speed (N) = 1300rpm Reading 1 2 3 4 5 6 7 8 9 10 11 Q(m3/s) 0.1879 0.17 83 0.16 81 0.15 73 0.14 58 0.13 32 0.11 93 0.10 35 0.08 48 0.06 07 0.01325 Pump Speed (N) = 1400rpm Reading 1 2 3 4 5 6 7 8 9 10 11 Q(m3/s) 0.2014 0.19 06 0.17 92 0.16 71 0.15 40 0.13 96 0.12 5 0.10 52 0.08 27 0.05 13 0.01325

Table 10: Discharge Values across the Pipe for the Three Different Pump Speeds The amount of hydraulic power (PH) (in joules), electrical power (PE) in watts and the efficiency (η) generated by the pump at each operating speed is given by the relations

 

, PE = Amps x Volts, and

   

where

and g are density (1000kg/m3) and gravity (9.81m/s2) respectively. Q and Hm values for each pump speed are given in tables 5 and 4 respectively, No. of Volts = 415. Amps values are given in table 1, while PH and PE values are given in table 6

Pump Speed (N) = 1200rpm Readings 1 2 3 4 5 6 7 8 9 10 11 PH(joules) 3189 3762 3911 3966 4263 4309 3931 3367 2684 1960 1001 PE(watts) 6640 7055 7474 7719 7885 7470 7055 7263 7055 7470 1224 3  η (%) 48 53.3 52.3 51.4 54.1 57.7 55.7 46.4 38.1 26.2 8.18 Pump Speed (N) = 1300rpm PH(joules) 2700 3113 4805 5663 5970 5783 5327 4622 4702 3761 968.4 PE(watts) 6848 7263 7678 7885 8300 8923 9130 8715 8093 8715 1162 0  η (%) 39.4 42.9 62.6 71.8 71.9 64.8 58.3 53.0 51.9 43.2 8.33 Pump Speed (N) = 1400rpm PH(joules) 3019 4271 5123 6842 6687 5026 6200 5348 4306 3242 1198 PE(watts) 7678 8715 9130 9960 10165 10375 10168 9753 9545 11205 1245 0  η (%) 39.3 49.0 56.1 68.7 65.8 48.4 60.9 54.8 45.1 28.9 9.62

Table 11: Values of PH, PE, and η for each of the Three Pump Speed

The values in tables 5 and 6 implies that at each pump operating speed, the hydraulics power, electrical power and the efficiency of the pump follows a variable sequence. That is, the values increase decreases and latter increases. This is replicated in the graphical relationships between these parameters. The pump speeds also affects the flow rate.

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Figure 3: Graph of Hm (m) Against Q (m3/s) 0 10 20 30 40 50 60 70 80 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 0.16 0.18    E    f    f    i  c    i  e  n   c   y    (    %    ) Q (m3/s) η (%) Vs Q (m3/s) η (%)1200 η (%)1300 η (%)1400 0.112 0.084 0.143 0.16 0.086 0.118 0 1 2 3 4 5 6 7 8 9 10 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 0.16 0.18    H  m    (  m    ) Q (m3/s) HmVs Q Hm1200 Hm1300 Hm1400

iso - efficiency lines

1300rpm 1400rpm 0 1000 2000 3000 4000 5000 6000 7000 8000 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 0.16 0.18    P   H    (    j  o  u    l  e  s    ) Q (m3/s) PH Vs Q PH1200 PH1300 PH1400

Figure 1: Graph of Efficiency (%) Vs Discharge (m3/s)

Figure 23: Graph of PH (Joules) against Q (m3/s)

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Figures 1, 2 and 3 above shows the characteristics performance curve of the pump for the Head (Hm), Hydraulic power (PH), and Efficiency ( η (%)) against the Discharge (Q m3/s) for each of the three pump speeds. The curve at each figure does not follow a consistent format, as it varied without a regular rythm.This may be due to experimental error. It can be shown that axial pumps provide higher head but lower discharge. This factor can thus affect the use of axial pumps in some application. Figure 2 explains the effect of a decreasing flow rate as it increases the momentum force of the motor. The efficiency on the pump increases until a point before starting to decrease. The iso  – efficiency lines shows the efficiency of the pump at a given pump speeds.

For N = 1200rpm,Hmat 1200rpm (table 2) H1200 2.032 2.536 2.788 3.04 3.292 3.922 4.048 4.048 4.048 4.552 7.702 For N = 1300rpm,Hm at 1300rpm (table 2) H1200 1.248 1.517 2.483 3.127 3.557 3.771 3.879 3.879 4.308 5.382 6.348 For N = 1400rpm,Hm at 1400rpm (table 2) H1200 1.123 1.678 2.141 3.067 3.252 2.696 3.715 3.809 3.899 4.733 6.769 For N = 1200rpm,Q at 1200rpm (table 3) Q1200 0.160 0.1512 0.143 0.133 0.123 0.112 0.099 0.0848 0.0676 0.0439 0.01325 For N = 1300rpm,Q at 1300rpm (table 3) Q1200 0.173 0.164 0.155 0.145 0.135 0.123 0.11 0.095 0.078 0.056 0.0122 For N = 1400rpm,Q at 1400rpm (table 3) Q1200 0.173 0.163 0.154 0.143 0.132 0.119 0.107 0.091 0.071 0.044 0.011 For N = 1200rpm,PHat 1200rpm (table 4) P1200 3189 3762 3911 3966 4263 4309 3931 3367 2684 1960 1001 For N = 1300rpm,PHat 1300rpm (table 4) P1200 2124 2448 3779 4454 4696 4548 4190 3635 3698 2958 761.7 For N = 1400rpm,PHat 1400rpm (table 4) P1200 1901 2690 3226 4309 4211 3165 3904 3368 2712 2042 609.8

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Figure 4: Graph of H1200 (Joules) against Q1200 (m3/s)

Figure 5: Graph of Q (m3/s) against P1200 (joules)

Figures 4 and 5 show the respective relations between the Head and the power  output against discharge when the pump is operating at a constant speed of  1200rpm.There are not much differences between performance curves of the pump when the pump is operating at different speeds (figs.1, 2, 3 ) and when set at a base speed of 1200rpm (4, 5). The formal depicts the irregularity of the flow at each head while the later shows a near constant straight line and a varying flow rate as the momentum of the motor increases.

4 SOURCES OF ERROR

Due to the complexity of the experiment, the probability that errors are likely to be made/occur are highly likely, especially at the calculation part of the report. Sources of errors include reading the manometer (parallax), stiffness of the gate valve thereby slowing the process, sudden stoppage of the AC motor due to overheating.

0 1 2 3 4 5 6 7 8 9 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 0.16 0.18    H    (  m    ) Q (m3/s) H Vs Q H1200 H1300 H1400 0 500 1000 1500 2000 2500 3000 3500 4000 4500 5000 0 0.02 0.04 0.06 0.08 0.1 0.12 0.14 0.16 0.18    P    '    S Q (m3/s) P Vs Q P1200 P1300 P1400

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But that notwithstanding, accurate measures where applied during the experiment, and the results gotten as well as materials and method are still valid and the report a resourceful piece of material.

5 CONCLUSION

The experiment was a success and the results gotten fairly ok because they are within the range of the experimental expectation.

From table 1, the results for the manometers readings and the currents tends to follow a similar pattern of varying values for the three pump speeds. The same scenario follows for the hydraulic heads of the pump at each pump speed. As the speed increases from 1200 rpm to 1400rpm,the values of the head (Hm),manometer  readings ,discharge, hydraulic power ,efficiency ,electrical power and all other  parameters involved increases initially, then maintains a near constant value at the middle then finally decreases.

The plots obtained for the pump performance curves was as result of the experimental values, which was quite (curve) unexpected due to the irregularity of  the values obtained for the head and the discharge. The efficiency of the pump tends to increase as the speed increases (fig.3).

Hence, in general the performance of the pump was fairly ok with an average percent (50-60%) of efficiency.

6 REFERENCES

1) Laboratory Report Instruction Sheet/Manual By Dr.Kaiming She 2) A.J Chadwicket al : Hydraulics in Civil and Environmental

Engineering, 4th Edition, [P.205, 209], Spon Press, 2005. 3)

References

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