Structural Engineering Centrifugal Pump Test Laboratory Engineering Essay

Structural Engineering outward-bound-developing eye probeing lab Engineering EssayThis report examines the go(a) handle. Firstly by examining the clay mode send peculiarity, then by examining the erects varying the aim rush along has on a genius pith. Finally the report examines and comp bes the handling of deuce piths in serial and then in replicate.Theoretically examination of the establishment ear characteristic should topic a graphical record of schema fling against record flow raterate which is moldd, the curve should begin supra zero from the y axis, due(p) to dormant lift.Theoretically examination of the effect of varying push urge on crossways a administration of a wizard mettle should collection that higher(prenominal)(prenominal) ride expedites lead to higher efficiency in the wield placement along with big assortments of force-out across the placement, and a larger spue in head values.Finally comparison of a scheme with two hearts procedured in serial publication and in analog should submit that the method used pull up stakes not have an effect on the efficiency of the system. However it should also show that the system in series has doubly the head values of that in parallel and that the system in parallel has in two ways the rule book flowrate values of the system in series. general they should have the same Mass flow.Upon comparison of the results obtained with theory, it is evident that for the most part, the data-based results agree with theory. Any minor disagreements betwixt theory and auditionation will be explained in the discussions and conclusions section of this report.This report serves to display knowledge and dread of the operation of a push(a) affection gained from completion of the experiment.IntroductionThe determination of this lab is to study the operation and cognitive process of a centrifugal gist. outward-moving cores ar an example of a liquid machin e. Fluid machines be devices that depute vital force to or from a nomadic. Fluid machines include spunks, fans and compressors. This experiment deals with a heart and soul. gists are devices used to move gases or liquids from lower to higher pressure. The diversity in pressure is overcome by adding talent to the system. Specifically, centrifugal eyes ensnarl by converting rotational kinetic energy into hydro dynamic energy. The rotational energy is typically supplied by an engine or electric beat back or turbine. force back(a) middles are an important machine to study from an engineering pip of view as they are very widely used as a promoter of delivering liquids. Centrifugal philias are used in handle such as sewage, petroleum and petrochemical tendernessing.For the purpose of this report the centrifugal nub was studied in terms of its performance when a wizard pump was used and also when two pumps were used ( both(prenominal) in series and in parallel). The pur pose being to highlight the set up this had on results. The system characteristic was also investigated. The overall purpose of this experiment is to give a purify understanding and insight into how this fluid machine works. infra is an image of a centrifugal pump. A greater insight into how it operates and an explanation of the function of the sundry(a) parts will be provided later in the report.http//www.pumpfundamentals.com/images/closed_impeller.gifFigure 1 Centrifugal Pump Diagram 1ObjectivesThe primary aim of this laboratory is to gain a better understanding of pumps, in particular the centrifugal pump. Insight is gained into the principles of operation of a centrifugal pump and the process through and through which a pump transfers energy to a fluid system.There are three parts to this experimentTo determine the system characteristic for the fluid system on which the pump operates.To determine the performance of a wiz pump relative to travel stimulate.To determine (f or a bushel labor fixture) the performance of two centrifugal pumps run in series (ii) Operating in parallelTheoryBasic theory and workings of Centrifugal pumpAs previously stated, the principle operation of a centrifugal pumpis to convert fluid velocity into pressure energy.The pump is do up of three comp whizznts the inlet duct, theimpeller, and the volute.http//htmlimg2.scribdassets.com/4sp8x32v9cejngi/images/4-dd8b7539b4.jpgFigure 2 Centrifugal Pump Diagram 2Fluid enters the inlet duct (D).As the slit (A) rotates, the impeller (B), which is affiliated to the shaft, alsorotates.The impeller consistsof a number of bladesthatproject the fluid outward when rotating.This centrifugal force gives the fluid a high velocity.Next, the moving fluid passesthrough the pump case (C)and then into the volute (E).The volute househas a uniformly increasing area.This increasingarea decreases the fluidsvelocity, which converts thevelocity energy into pressure energy. 2Determining the form peculiar(prenominal)The first amount of the experiment is to identify the system characteristic of the pump.When a pump is fitted in a system, it is tested so as to ensure that the volume flow-rate and head of the pump are within required specifications. The flock flow rate mountain be defined as the volume of the fluid that passes through a given surface per unit time, and the head of the pump is a measure of the fluid energy.In pronounce to do this we must acquire the pump head and the volume flow rate. We then plot the pump head (expressed in metres) against the volume flow rate (expressed in m3/s). This should yield a curve.The system head characteristic is dependent on static lift which is associated with change in elevation of the fluid, contraction or elaborateness of the fluid associated with acceleration and deceleration of the fluid, and the losses within the system. Below is a theoretical graph, showing how the curve should appear.http//www.climatechange.gov.au/wha t-you-need-to-know/appliances-and-equipment/electric- rams/system-optimisation/optimising-pump-and-fan-applications//media/Images/electric-motor/system-curve.ashx?w=447h=324as=1Example graph for system head characteristic3When a pump is attached to a system the operating point occurs when the pump head hpump equals the system head hsystem. The best operating conditions occur when the required duty point of head and flow intersects the operating point and the design point, the point of maximum efficiency. single(a) Centrifugal Pump CharacteristicsThe next aspect of the experiment is to determine the performance of a single pump as a function of motor whet. The performance of a pump is generally mapped by plotting pump head (hpump), galvanizing spot (Pelectric) and pump efficiency (pump) as a function of the volume flow rate Q through the pump.The use of a single pump is investigated for three different motor fixednesss, measuring the effect varying the motor speed has on pump he ad, electrical force play and efficiency. These values are then plotted on a graph against the volume flow rate.TheoreticallyHigher speeds yield higher efficiencyHigher motor speeds lead to a larger change in violence across the system.Higher motor speeds yield higher head values (expressed in metres).Double Centrifugal Pump CharacteristicsThe final aspect of this experiment is the probe of the effects of the use of two centrifugal pumps on the system. The pumps are dictated in series and then in parallel. Both systems, i.e. the pump system which is in series and that which is in parallel are set to the same motor speed. In both cases head, electrical proponent and efficiency are metric and plotted against volume flow rate. The graph for the system in series can then be compared to the graph for the system in parallel, in coiffure to study and compare the different systems.Centrifugal pumps both in series are used to overcome larger system head loss than one pump can handle a lone, whereas centrifugal pumps in parallel are used to overcome larger volume flows than one pump can handle alone.4When running in series, the heads are added and the total capacity is equal to that of the pump with the smallest capacity, whereas in parallel, the capacities of the pumps are added, and the head of all pumps will be equal at the point where the laid-off liquids recombine.5Theoretically whether the system is in series or in parallel shouldnt affect the efficiency of the system.Experimental MethodsEquipment Used-The primary piece of equipment used was the centrifugal pump, a detailed explanation of its operation can be free-base in the theory section of this report (see page 6).We also use a differential pressure transducer, which is a type of pressure sensor.We use a computer to measure and record data.Methods-System brainiac Characteristic bluff valve V1 and close valve V2 located in the inlet grapevines to pumps 1 and 2. termination valve V3 which connects the re farm pipeline from pump 1 to the inlet pipeline to pump 2 surface valve V4 located in the outlet pipeline from pump 1.Open the discharge valve V5 to just about 75% of its fully opened position. disjunction the low pressure line connecting differential pressure transducer to upstream of pump 1.Record the motor speed, the discharge volume flow rate, the pressure measured by the differential pressure transducer and the system head.Increase the speed of motor 1 incrementally, at each increment repeat the above measurement and continue to do so until the motor speed had reached its maximum.Plot the system head characteristic against volume flow rate. bingle PumpOpen valve V1 and close valve V2 located in the inlet pipelines to pumps 1 and 2. penny-pinching valve V3 connecting the outlet pipeline from pump 1 to the inlet pipeline to pump 2Open valve V4 located in the outlet pipeline from pump 1. cozy fully the discharge valve V5.Set the speed of the motor connected to pump 1 using t he motor speed controller to 45 HzRecord the saturation flowrate Q, the pump head hp, the electrical function consumed Pelectrical and the pump efficiency pump.Open valve V5 incrementally, at each increment ingeminate the above step and continuing until the valve is fully opened.Plot pump head, electrical power and efficiency against volume flow rate Q at that motor speed. parallel the procedure for motor speeds of 35 and 40Hz.Double PumpIn serial publicationOpen valve V1 and close valve V2 located in the inlet pipelines to pumps 1 and 2.Open valve V3 connecting the outlet pipeline from pump 1 to the inlet pipeline to pump 2.Close valve V4 located in the outlet pipeline from pump 1.Close fully the discharge valve V5.Set the speed of the both motors connected to pump 1 2 to 45 Hz using the motor speed controller.Record the volume flowrate Q, the pump head hp, the electrical power consumed Pelectrical and the pump efficiency pump.Open valve V5 incrementally, at each increment repe ating the above step and continuing until the valve is fully opened.Plot pump head, electrical power and efficiency against volume flow rate Q at that motor speed.In ParallelOpen valve V1 and close valve V2 located in the inlet pipelines to pumps 1 and 2.Open valve V3 connecting the outlet pipeline from pump 1 to the inlet pipeline to pump 2.Close valve V4 located in the outlet pipeline from pump 1.Close fully the discharge valve V5.Set the speed of the both motors connected to pump 1 2 to 45 Hz using the motor speed controller.Record the volume flowrate Q, the pump head hp, the electrical power consumed Pelectrical and the pump efficiency pump.Open valve V5 incrementally, at each increment repeating the above step and continuing until the valve is fully opened.Plot pump head, electrical power and efficiency against volume flow rate Q at that motor speed.Experimental ResultsSystem characteristic for the fluid systemBelow is the circumvent of results for the determination of the sy stem characteristic for the fluid system get speed N (Hz)Vol FlowrateQ(m3/s)Psystem PaHsystem (m)1400.7160.123333210.1886673.2230.376667250.3683334.2966670.486667320.4776676.9110.753333350.5456678.4506670.91390.64766710.061671.073333420.71412.711671.346667470.79633314.931671.573333The graph for the system characteristic (Hsystem against Volume flowrate) is beneathGraph 1 (System Characteristic)Single Pump TestSingle Pump Test for Motor Speed 45 Hz-Below is the table of results for the single pump test at a motor speed of 45HzVol Flowrate Q(m3/s) conduct (m)Efficiency % force out W08.7866670109.943308.4433330109.0507.1166670116.863306.980130.533307.3066670163.250.2463337.329.7181.88670.3326677.18666711.9197.020.4273337.01666714.3205.64670.5376.83333315.93333226.07330.6196676.3816.53333234.21330.7383335.87666717.1249.18670.7813335.70333316.76667260.4133The corresponding graphs for the single pump test at motor speed 45Hz are below summarize MotorPower (W)Single Pump Test for Motor Sp eed 40Hz-Below is the table of results for the single pump test at a motor speed of 40 HzVol Flowrate Q(m3/s)Head (m)Efficiency %Power W06.2518680128.01310.3763335.40666710.96667178.87330.555.1913.4208.57670.6754.70666713.7226.72670.73354.52513.7237.915The corresponding graphs for the single pump test at motor speed 40Hz are belowTotal MotorPower (W)Single Pump Test for Motor Speed 35 Hz-Below is the table of results for the single pump test at a motor speed of 35 HzVol Flowrate Q(m3/s)Head (m)Efficiency %Power W0.0544.7224341.633333118.00140.3056674.2766677.066667170.90.5923.659.666667218.180.6323333.5466679.666667226.31670.6303333.3433339.166667225.1767The corresponding graphs for the single pump test at motor speed 35Hz are belowTotal Motor Power (W)Double Pump TestSystem in series-Below are the results of the two-baser pump test for a system in series-Vol Flowrate Q(m3/s)Head (m)Efficiency %Power Motor 1 (WPower Motor 2 (W)Total Motor Power (W)018.213330109.293355.99165.2833015 .380128.416754.69183.10670.25566714.8033315.16667181.316762.82667244.14330.4314.3866723.5201.006757.37258.37670.53766713.7066726.7218.6751.43270.10.61866713.0826.86667240.396754.44333294.840.73033311.6526.96667256.186752.89667309.08330.8526679.82666725.06667272.623354.68667327.310.8833339.86333325.16667278.1660.62667338.7867The corresponding graphs for the double pump test for a system in series are belowTotal Motor Speed (W)System in parallel-Below is the table of results for the double pump test for a system in parallelVolume Flowrate Q (m3/s)Head (m)Efficiency (%)Motor Power 1 (W)Motor Power 2(W)Total Motor Power (W)09.196670111.32763.8833175.210.2777.611134.84752.49187.33670.471677.6717.3144.77360.1367204.910.5987.4166720.1333152.91762.7467215.66340.720337.3366722.8333165.44361.28226.72330.836337.3966727171.0653.3867224.44670.970337.1166727.7191.24352.7333243.97661.116336.8528.3667201.33762.7433264.081.297676.7066731.9667210.61356.2367266.851.376676.3329.9667228.59755.6633284.26 1.5546.0266730.9241.2159.4867300.69671.630335.7330244.1460.7933304.9333The corresponding graphs for the double pump test for a system in parallel are belowTotal Motor Power (W)Discussion ConclusionsThis section of the report contains a discussion of the results obtained along with conclusions drawn from said results and also where necessary, comments regarding any un evaluate values.System Head CharacteristicThe first part of the experiment was conducted in order to detect a system head characteristic curve. Volume flowrate, measured in m3/s, was mapped against Head, which is measured in metres. We would persuade this to yield a smooth curve startle above the zero mark form the y- axis, in order to allow for static lift in the pump system.As expected the system head characteristic was found to be a curve, starting slightly above the zero mark on the y axis, indeed for the most part, results were conclusive with theory. However there is one discrepancy between expected results a nd the actual results obtained, as the curve is not entirely smooth. some possible reasons for the slightly irregular shape of the curve areSingle Pump TestThe second part of this experiment was to investigate the effect changing motor speed has on a pump. In order to conduct this investigation pump head (hpump), electrical power (Pelectrical), pump efficiency (pump) and volume flowrate (Q) were measured for a variety of motor speeds. thusly hpump, Pelectrical and pump were mapped against Q for each motor speed. The reason for this being to highlight the effects changing motor speed has on the centrifugal pump system. We expect firstly that higher motor speeds yield higher efficiency, secondly that higher motor speeds lead to a larger change in power across the system and finally that higher motor speeds yield higher head values.Upon studying the results of the experiment we can see that they match up with theory.Efficiency-Theory- Efficiency, simply put, refers to how well a pump can convert one form of energy into another. In this case how well the pump converts rotational kinetic energy into hydrodynamic energy. The overall efficiency of a centrifugal pump is defined as the ratio of the pissing (output) power to the shaft (input) power. By increasing the speed at which the motor rotates the shaft, the shafts power is increased, thereof the value of efficiency is increased.Results- Higher motor speeds did in the case of this experiment did yield higher values for efficiency. For a motor speed of 45 Hz the highest efficiency value obtained was approximately 16.7%, for a motor speed of 40Hz Hz the highest efficiency value obtained was approximately 13.7% and finally for the lowest motor speed used, 35Hz, highest efficiency was approximately 9.16%.Power Change-Theory- Power can be defined as a work/time ratio. The work in the case of this experiment is the rotation of the shaft by the motor, which in turn creates a centrifugal force in the water. For a faste r motor speed, the shaft rotates faster, meaning that more work is done per unit time. This means a greater rise in the power value.Results- In this experiment, as expected, higher motor speeds yielded larger changes in power across the system. For a motor speed of 45 Hz the rise in power in across the system was approximately 150.47 watts. For a motor speed of 40 Hz the rise in power in across the system was approximately 109.9 watts. Finally, for the lowest motor speed used, 35 Hz, the change in power in across the system was approximately 107.18 watts.Head-Theory- Head is the height at which a pump can raise water up. The higher the value of pressure, the higher the value of head will be. Since facelift rotational speed strongly affects pressure loss of a fluid, we can see that it also affects head loss. Results- In this experiment, as expected, higher motor speeds lead to a greater loss in head (measured in metres) across the system. For a motor speed of 45 Hz the tumble in he ad across the system was approximately 3.09 metres. For a motor speed of 40 Hz drop in head across the system was approximately 1.727 metres. Finally, for the lowest motor speed used, 35 Hz, drop in head across the system was approximately 1.38 metres.Double Pump TestThe final part of the experiment was to investigate (for a fixed motor speed) theperformance of two centrifugal pumps firstly operating in series and secondly operating in parallel. The two results for the system in series and for the system in parallel could then be compared. In order to conduct this investigation pump head (hpump), electrical power (Pelectrical), pump efficiency (pump) and volume flowrate (Q) were measured, firstly for the system in series and secondly for the system in parallel.Theoretically, when both systems are set at the same motor speed, the pump in series should have twice the Head value of the system in parallel, whereas the system in parallel should have twice the volume flowrate of the syste m in series. Meaning that both systems end up with the same mass flow. Whether the pumps are in series or in parallel should have no effect on the efficiency of the system.Head-Theory-Results- As expected the system in series has approximately twice the head value of the system in parallel. (Series18.22m Parallel 9.2m)Volume Flowrate-Theory-Results- As expected the system in parallel has approximately twice the volume flowrate value of the system in series. (Series 0.883 Parallel 1.63)Mass Flow-Theory-Results-Efficiency-Theory-Results-