Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

download Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

of 12

Transcript of Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    1/26

     

    CEE410 

    Lab  Assignment  #2 

    Flow Measurement  Testing 

    NOAH DUFOE‐GUILES 

    VANNA LIU 

    CRAIG SNORTHEIM 

    JACQUI GERMAN 

    November 26, 2014 

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    2/26

    Introduction

    Testing and calibration of flow meters is important for understanding the true volumetric flowrates in pipes so that a proper system analysis can be conducted. In this lab, we recordedreservoir tank elevation data and flow meter data at Unit Well 30 within the Madison WaterUtility district. Two types of flow meters were used: an acoustic (ultrasonic) flow meter, and amagnetic flow meter. The pump frequency was set to five different levels, and then turned backto full power while a control valve was progressively shut to three different levels. At each flowlevel, a steady flow rate was established by the pump operator, and flow and tank elevation datawas were recorded. With this data, we were able to compare the ‘true’ flow rate (change in tankvolume over time) to the readings on the flow meters. We averaged the measured flow rates thatfell into each interval, and assumed the ‘true’ flow rate was constant within a given interval. Inreality, the flow would change slightly was as the NPSH was changing over time. Our analysis

    of the accuracy of the flow meters and the ensuing recommendations follows.

    Literature Review

    The selection of water and pressure sensors as well as flow meters is a detailed process.Environment Environmental conditions are considered (i.e. temperature, humidity, gases)however, adequate ventilation assists in minimizing the effect of many of these. Modern devicescan be useful in the sense they are generally more detail with up-to-date technology. Although,these unique instruments generally also require more highly skilled specialists for servicing andinstallation. Another important consideration that Bosserman et al. (2008) states is that,“Instrument systems usually consists of a number of interdependent elements, each of which

    contributes to the total measurement of error, therefore errors are generally greater than the ones published in manufacturers literature,” (20.4). Pumping station instruments are selected to provide long lifespan, low maintenance, and high reliability in damp, corrosive environments.This selection process is specifically important to pumping stations as they are generallydesigned with a minimum lifespan of 20 years or more without major construction (Bosserman et

    al., 2008). This literature review goes over pressure sensors, elevation sensors, and flow metersin the Unit Well 30 design as well as ones in the market.

     Pressure Sensors

    The pressure sensor or transducer also takes on the name pressure transmitter. This device

    converts pressure into an analog electrical signal. This differs from discrete signals, whichreports a true/false signal (e.g. open/closed, running/stopped). These devices can be designed tofunction immersed in liquid and these are defined as submersible pressure transducers (Omega,2014).

    Submersible pressure transducers have been around since the 1960s and are documented to beinvolved in the Unit Well 30 design (exact design is undetermined). They were developed torecord water level and pressure data. Combined with other pressure data collecting devices (e.g.

     piezometers, tensiometers) these tools aid in providing continuous data. Differential pressuretransducers measure with respect to a varying pressure reference (e.g. ambient atmospheric

     pressure). Freeman et al. (2004) evaluate evaluated the standard for USGS pressure transducer performance in terms of accuracy with error brackets (+/- 0.01 ft or 0.1 percent of expected

    Commented [g1]: This is a good introduction  but a sentence that starts with something like “the purp

    this report is to …” 

    Commented [g2]: Try to use third person. 

    Commented [g3]: The word “data” is usually plur

    Commented [g4]: This would actually be the totadynamic head because reservoir elevation in the sys

    also changing.  So, the discharge and suction elevati

    both 

    changing 

    with 

    time.

    Commented [g5]: I’m not sure what you are sayinbut I can guess.  In my experience, the primary diffe

    over time has been the ability of  sensors to continuo

    send electronic output to a supervisory control and 

    acquisition  (SCADA) system.

    Commented [g6]: “however” would be a better where. 

    Commented [g7]: Indeed, it is  just as important founderstand the uncertainty in a set of  measuremen

    for us to understand the central tendency of  those 

    measurements. 

    Commented [g8]: Simultaneously  using “minimu“or more” is usually confusing to the reader. 

    Commented [g9]: Do we know how this device sepressure and then converts that to the analog signal

    Commented [g10]: I’m not clear what this word ireferring to here.  Is it referring to the device or to t

    analog electrical signal? 

    Commented [g11]: Good  – they perform both eleand pressure measurements. 

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    3/26

    range) for most water level application. Omega (2014) recorded a high accuracy pressuretransducer in their inventory with an error percentage as low as 0.05% (stating the average

     pressure transducer is around 0.25%).

    There are a couple pressure transducers that areassumed not to be included in the Unit Well 30 system.The C-Shaped Motion-balance Bourdon-tube is utilizedfor measuring pressure (see figure 1; Freeman et al.,2004). As pressure increasing increases in the Bourdontube, the tube displaces a linear voltage differentialtransformer (LVDT). This system is generally not

     preferred as it supplies a significant amount of wear onthe equipment and therefore decreases the incentives forusage (Bosserman et al., 2008). See Appendix C for amore detailed table of wastewater and clean waterapplication applications for pressure sensors.

     Elevation sensors

    Float sensors provide a means of measuring liquid elevation. These devices involve a buoyant body that remains at the liquid surface. Generally it is connected to a cable contraption thatallows free range in vertical direction, but restricts the range in the horizontal plane. This cableis then connected to a rod, possibly by means of a magnet, and as the system moves the magnet itactuates a switch returning feedback as to the level the liquid has reached.

    Floaters are frequently used in wastewater applications however containbut have a few

    disadvantages. Difficult to adjust, maintenance requiring access, and the wearing on the cable(2-3 years lifespan) are among the drawbacks. Due to likely debris in wastewater conditions

    these devices are made larger than in the clean water industry and are generally not preferred.

    Float switches are believed to be utilized at Unit Well 30 as stated in the design drawings. They provide a backup data feed to assist in calibration and data analysis.  A very simplistic drawingof this device can be viewed in figure Figure 2. Specifically the example model’s performance(selected in figure Figure 2) is rated for is maximum current, frequency range, and the number ofmicro disconnect automatic life cycles (HCP Pump, 2011). These switches also aid in insuringthat the water level does not fill past a designated elevation or does not drain past a designated

    elevation.

    Figure 1:  Diagram of  a C ‐shaped  Bourdon  pressure 

    transducer  (slightly  modified   from Freeman et  al., 

    2004) 

    Commented [g12]: Ok.  Considering your earlier statement, it is probably higher than this in real‐wor

    application.  Also, manufacturers will sometimes co

    apples with oranges to make their case.  In this case

    average might be in the field where their own data m

    in well‐controlled  laboratory  conditions.  Always con

    manufacturer statements when you begin working a

    engineer. 

    Commented [g13]: Ok, so what does the LVDT do

    I see

     how

     this

     device

     works.

     I’m

     not

     clear

     how

     the

     p

    device works. 

    Commented [g14]: On what equipment? 

    Commented [g15]: Nice summary. 

    Commented [g16]: This could be better written. 

    Commented [g17]: This is helpful. 

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    4/26

     

    Figure 2: Diagram depiction of  how  a  float  switch operates (HCP Pump, 2011). 

    Floaters remain on the surface of the liquid while displacers remain below the surface. Displacerinstruments are selected to be denser than the liquid submersed in and are accompanied with aspring related system the displacer adjusts with the changing liquid level. Again the device isrestricted in its motion in the horizontal and allowing free range in the vertical. Theseinstruments are preferred in wastewater application due to their inherent washing as the devicecontinues to be used decreasing maintenance. See Appendix C for a more detailed table of

    wastewater and clean water application.

     Magnetic flow meter

    Magnetic flow meters operate under the principle of Faraday’s Law of ElectromagneticInduction, which states that voltage generated in a conductor, E , is proportional to the velocity ofthe conductor, v, magnetic field strength, B, and length of conductor, D (equation 1, figure 3).

    The conductor, in this case, is the liquid measured.

    ∝ ∗ ∗   (1)The magnetic flow meter induces a magnetic field onthe fluid of a known strength, and as the fluid movesthrough the magnetic field, a voltage signal isgenerated according to Faraday’s Law. Electrodeson the pipe walls sense this voltage and an electronictransmitter calculates the velocity of the moving fluid

    (Instrumart, 2014).

    There are several requirements with the use ofmagnetic flow meters in the fluid measured and

     placement of the meter. The fluid has to be aconductive liquid, so conduits in de-ionized water,

    hydrocarbon or gaseous service cannot be measured by a mag meter. In addition, the flow metermust be placed downstream of 3-5 diameters and upstream of 0-3 diameters straight run. Thisassures that the flow through the meter is laminar, assuring the most accurate measurements.

    Figure 3. Operating  principle of  magnetic  flow  

    meters (Universal  Flow  Monitors, 2014). 

    Commented [g18]: I’m not sure what this is refer

    Commented [g19]: This is a nicely written section

    Commented [g20]: Can mag meters be used in tuflow conditions?  If  yes, then “laminar” isn’t quite th

    word. 

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    5/26

    According to Bosserman et al. (2008), magnetic flow meters are one of the most accurate flowmeters available. The vendors typically report an accuracy of 0.5% of flow, but, “in situverification of calibration” (20.13) is critical, as with installation of any flow meters. In theexperiment conducted at Unit Well 30, this flow meter was used to measure the discharge of

    Booster Pump #2.

    Ultrasonic flow meter

    Ultrasonic flow meters operate by the DopplerEffect, where frequency shifts of an ultrasonicsignal is are directly proportional to thevelocity of the fluid. Equation 2 explains thisrelationship, whereby f 1 is the frequencyinjected by the transducer, f a is the reflectedfrequency off bubbles or discontinuities in

    flow, v is the velocity of ultrasonic wave in thefluid, and s is the velocity of the fluid(Bosserman et al., 2008). This relationship

    can be seen pictorially with the figure Figure 4.

           (2)

    Similar to the magnetic flow meter, the advantage to the ultrasonic flow meter is that they arenonintrusive to conduit flow. An added benefit is that they can also be portable, as is the case in

    the experiment conducted at Unit Well 30 (Smart Measurement, 2012). There is no probe thatneeds insertion, and no direct contact with the fluid is necessary for measurement.

    With an error of up to 20%, ultrasonic flowmeters are not used in applications where accuracy iscritical. They are employed for wastewater service, as wastewater contains the “discontinuities”necessary for waves to reflect off of. Drinking water does not generally contain, “reliable

    reflective surfaces” (Bosserman et al., 2008).

    Venturi flow meter

    Figure 5: Operating  principle of  venture  flow  meter  (Fluid  Mechanics, n.d.). 

    Conservation of energy and Bernoulli’s equation are the governing principles for venturi flowmeters. When a fluid travels from a larger cross-sectional area through a smaller area, pressure

    Figure 4. Operating  principle of  ultrasonic  flow  meters (Smart  

    Measurement, 2012). 

    Commented [g21]: This was the primary purposelab report. 

    Commented [g22]: This figure could better explaEquation 2. 

    Commented [g23]: And why is this an advantage

    Commented [g24]: Ok, I’m now curious how yourcompare.

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    6/26

    increases proportional to the change in area. The pressures are read from the pressure taps a andb in figure Figure 5. However, energy and flow at both points must remain the same. Usingequation Equation 3, which combines conservation of energy and Bernoulli’s equation, and

    equation Equation 4, a mass balance, the flow can be solved for (Sleigh & Noakes, 2009).

    ∆  

      (3)

     

      (4)In contrast to the two previously discussed flow meters, the venture venturi flow meter doesmaintain direct contact with the fluid. However, according to Bosserman et al. (2008), “headrecovery is excellent,” (20.14). That is to say the venturi flow meter does not disturb the flowsuch that it loses much energy. Because of the meter’s shape, it can actually correct anyirregularity in flow through the conduit/meter (Bosserman et al., 2008). This can be useful when

    flow needs to measured where there is a very short straight run of pipe.

    According to Engineering Toolbox (n.d.), the venturi flow meter can be accurate up to 10% offlow if calibrated properly. This kind of meter is generally used for drinking water applications,

    as solids will disturb pressure measurements.

    Methods

    The pump was run at five different speeds as well as at full speed with the control valvemanually throttled at three different rates. Each of the pumping speeds were run long enough to

     produce accurate results, approximately long enough to pump the reservoir down one foot. Timeand water elevation data were collected at the beginning and ending of the flow rate period. Once

    the flowmeters stabilized multiple readings were collected from both the magnetic meter and theacoustic meter during each flow rate period. The flowmeter readings for each meter wereaveraged for each pumping speed.

    The time and elevation changes were used to calculate volumetric flow rates for each pumpingspeed. This rate was then compared to the average rates recorded for each flowmeter throughoutthe same period and percent error was calculated. The results can be seen in Appendix B.

    Conclusions and Recommendations

    The results of our analysis show that the flow meters were generally within -5% to 15% of the‘true’ flow rates calculated via tank elevation changes over time. The magnetic meter was moreaccurate (between -4.6% and 10.8% error) than the acoustic flow meter (0.2% to +16.9%), as isexpected. The mean error of the magnetic meter was +0.2% while the mean error of the acousticmeter was +5.7%, suggesting that the acoustic meter was biased and tended to overestimate theflow. The acoustic meter likely showed greater error because it has a lower accuracy (0.5% and20% for the magnetic and acoustic meters, respectively), and because it was placed in close

     proximity to a fitting which caused turbulence in the flow. The acoustic meter measurements fellwithin this accuracy range (+/- 20%), but the magnetic meter measurements did not (+/- 0.5%).

    Commented [g25]: Be very careful using this worengineer because it puts you at risk for unanticipate

    problems.  There are insurance companies that call t

    of  

    the 

    “forbidden 

    words” 

    in 

    legal 

    documents 

    such 

    asengineering reports. 

    Commented [g26]: Ok. 

    Commented [g27]: You didn’t use a venturi metelab but it would be calibrated with a similar approac

    Commented [g28]: What does this refer to?  Are saying long enough to produce an accurately measu

    elevation change in the reservoir?  

    Commented [g29]: Always provide a written sumresults in a lab report’s main body. 

    Commented [g30]: In retrospect, I should have asto look up the acceptable error listed in state law (th

    the section enforced by the Public Service Commissi

    Commented [g31]: I’m missing something here  –doesn’t seem consistent with the rest of  the paragra

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    7/26

    This suggests that either the magnetic flow meter was not operating correctly, or the ‘true’ flow

    rates are flawed.

    We suggest that the reason for the relatively high error in the magnetic flow meter measurementsis due to sources of error in measuring the ‘true’ flow rates. The flow rates are based on changein elevation in the tank (digitally displayed to tenths of feet) over time (recorded to accuracy ofone minute). There is notable error associated with the timing of reading the tank elevationchanges (length of time since last change in digital display) and recording the time with a devicethat had only minute accuracy. Therefore, the ‘true’ flow rates have some considerable error

    associated with them, and the error cannot be completely attributed to the flow meters.

    Given the uncertainty in the baseline flow rate data (derived from tank volume), we are notmaking any recommendations related to the operational state of the flow meters. Instead, werecommend a more rigorous test be conducted with the following changes: 1) time recorded witha stopwatch or device with second resolution; 2) times recorded at exact time of the elevation

    display changes; 3) longer time intervals at each flow. Alternatively, it might be helpful toutilize time-series elevation and flow data from the Utility if available. Finally, the portableacoustic flow meter should be placed as far from sources of turbulence (e.g. fittings, bends) as

     possible.

    Commented [g32]: This needs more explanation.

    Commented [g33]: Perhaps we can get data fromSCADA system. 

    Commented [g34]: Ok. 

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    8/26

    Bibliography

    Bosserman, B. E, Jones, G. M, Sanks, R. L, & Tchobanoglous, G. (2008). Pumping stationdesign. Rev. 3rd ed. Amsterdam: Elsevier/Butterworth-Heinemann.

    Fluid Mechanics (n.d.) “Applications of the Bernoulli Equation”http://www.efm.leeds.ac.uk/CIVE/CIVE1400/Section3/bernoulli-apps.htm Date Retrieved:

     Novemeber 22, 2014

    Freeman, L., Carpenter, M., Rosenberry, D., Rousseau, J., Unger, R., and McLean, J. (2004).Use of Submersible Pressure Transducers in Water-Resources Investigations Reston, Virginia;United States Geological Survey, Chapter A of Book 8, Instrumentation for Measurement ofWater Level.

    HCP Pump (2011). “Float Switch” http://www.hcppump.com.tw/English/Archive/SJE.htmlDate Retrieved: November 22, 2014

    Instrumart (2014). “Magnetic Flow Meters” https://www.instrumart.com/pages/223/magnetic-

    flow-meters Date Retrieved: November 23, 2014

    Omega (2014). “Pressure Transducers & Transmitters”http://www.omega.com/prodinfo/pressuretransducers.html Date Retrieved: November 22, 2014

    Smart Measurement (2012). “Ultrasonic Measuring Principle”http://www.smartmeasurement.com/Products/FlowMeters/Ultrasonic/MeasuringPrinciple.aspxDate Retrieved: November 23, 2014

    The Engineering Toobox (n.d.). “Types of Fluid Flow Meters”http://www.engineeringtoolbox.com/flow-meters-d_493.html Date Retrieved: November 23,2014 

    Universal Flow Monitors (2014). “Magnetic Flowmeter Technology”http://www.flowmeters.com/magnetic-technology Date Retrieve: November 22, 2014

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    9/26

    Appendix A

     Raw Data

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    10/26

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    11/26

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    12/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    13/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    14/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    15/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    16/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    17/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    18/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    19/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    20/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    21/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    22/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    23/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    24/26

     

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    25/26

    Appendix B

    Appendix C

    Figure 6: Pressure Measuring Elements (Bosserman et  al., 2008) 

    Figure 7:

     Level 

     Measuring

     Elements

     (Bosserman

     et 

     al.,

     2008) 

    Time 

    Period

    Elapsed 

    Time 

    (min)

    Change 

    Elevation 

    (ft)

    Change 

    Volume 

    (ft^3)

    Change  

    Volume 

    (gal)

    Flowrate 

    (gpm)

    Mag 

    Meter 

    (gpm)

    Mag 

    Meter 

    Error

    Acoustic 

    Meter 

    (gpm)

    Acoustic 

    Error

    1 10 1 3002 22455 2246 2197   ‐2.2% 2310 2.9%

    2 11 1 3002 22455 2041 2143 5.0% 2233 9.4%

    3 10 0.8 2401 17964 1796 1757   ‐2.2% 1848 2.9%

    4 15 1 3002 22455 1497 1440   ‐3.8% 1519 1.4%

    5 14 0.3 901 6737 481 468   ‐2.8% 497 3.4%

    T1 14 1 3002 22455 1604 1777.25 10.8% 1875 16.9%

    T2 22 1.4 4203 31437 1429 1363.222   ‐4.6% 1432 0.2%

    T3 17 0.8 2401 17964 1057 1070.375 1.3% 1152 9.0%

  • 8/19/2019 Gwh Feedback on Snortheim, Liu, Dufoe-Guiles, German

    26/26

    Appendix D

    Calculations

    ∆ 1:52 1:42 10  

    ∆ 17.3 16.3 1 

    ∆ ∆ ∗ 1 ∗3056 ∗ 7.48    22860 

     ∆∆  22860

    10   2286  

         2286 2207

    2286   3.5%