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Thread: Calculating volume of fluid discharged

  1. #16
    Leftyretro Excellent Leftyretro Excellent Leftyretro Excellent Leftyretro Excellent
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    I worked in process control plant for several decades and I'm familiar with lots of different flow meters. The different types all have advantages and disadvantages, as there is no perfect flow meter, trust me. If the measurement involves custody transfer ($$ changing hands based on reading) then either a positive displacement type flow meter or a corollas mass flow meter is normally used and it's calibration is usually validated by a 3rd party calibration service periodically. If just for in house use then a integral orifice differential pressure flow meter works well for the flow rate you mentioned. The temperature probe in the pipe method is not a very accurate measurement, we used them in safety showers to give a flow / no flow alarm that someone had activated the shower.

    A load cell can be a very accurate method but only works easily for batch type applications rather then continuous flow applications. Also note that flow and total mass quantity are two different measurements. A flow measurement would have to be integrated VS time to give totaled material quantity and be reset after each batch run. Using tank level drop for material added or removed can be quite complex as level instruments themselves vary in type and accuracy. Also many tanks are not perfect cylinders and have can have internal parts and structural pieces that require advance 'tank strapping' calculations to accurately compensate for measurement of material balance.

    So it really comes down to defining all your specification requirements before selecting the best method.

    Lefty
    Last edited by Leftyretro; 1st January 2009 at 06:59 PM.
    Measurement changes behavior


  2. #17
    ssylee Newbie
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    Quote Originally Posted by user_88 View Post
    Have you considered using an ultrasonic distance sensor, placed at the top of the tank, to read the height of the liquid within the tank, before and after a given process? It would be necessary for the tank to have a reasonably constant cross section .... top to bottom. Basically, ΔV=Acs×Δh.
    For the cost of an ultrasonic transmitter/receiver, and a microcontroller, you might be able to accomplish your objective. ....
    There is a subroutine for driving an ultrasonic range finder.
    It might be in this book .... not sure, I have the first edition.:
    The Quintessential PIC® Microcontroller (Computer Communications and Networks)

    Amazon.com: The Quintessential PIC® Microcontroller (Computer Communications and Networks): Sid Katzen: Books
    After taking a look at the prices of a variety of flowmeters, I'm not entirely sure if this solution would fit ideally in terms of cost considerations.

    For the ultrasound liquid level meter method, what are other limitations to take into account other than needing a container with roughly constant cross-sectional area?

    My specification is that I know about the change in water level after a feeding session (i.e. amount of water before feeding - amount of water after feeding). I hope this specification helps.

    Thank you all for your input.
    Last edited by ssylee; 2nd January 2009 at 03:32 AM. Reason: Missing Leftyretro's reply

  3. #18
    rjvh Excellent rjvh Excellent rjvh Excellent rjvh Excellent rjvh Excellent
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    How Accurate doe you need it to be

    a normal nivau meter (with a extra measure inputs and contacts in the tank) can give you already a a good visual indication how much you did use

    150L is not that much to store in my opinion so if you have 20 points that takes a level spaced evently from each other than you have a 7.5 liter acuracy of the closing of one contact/input

    you make these spacings smaler than you get in a sertain range even a bigger acuracy

    easyest to make and cheap (use some logic gates to couple the sensor wires in the tank)

    is it a hobby project or a comercial project where the info is used for $ calculations????

    Robert-Jan

  4. #19
    user_88 Newbie
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    Quote Originally Posted by ssylee View Post
    After taking a look at the prices of a variety of flowmeters, I'm not entirely sure if this solution would fit ideally in terms of cost considerations.

    For the ultrasound liquid level meter method, what are other limitations to take into account other than needing a container with roughly constant cross-sectional area?

    My specification is that I know about the change in water level after a feeding session (i.e. amount of water before feeding - amount of water after feeding). I hope this specification helps.

    Thank you all for your input.
    About the only factor that you need to consider is accuracy.
    .... seem like this was an end-of-chapter problem in the book ....
    I will have to check on it.

    I get the impression that the ultrasonic transducers are reasonably durable, and immune to corrosion .... They might require occasional cleaning if there is a buildup of dirt, sludge, or other residue.

    ... Not surprised at the cost of flow meters .....

  5. #20
    ssylee Newbie
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    This is more like an industrial project for research purposes. The solution needs to be able to withstand quite caustic environments, aka ammonia. In terms of accuracy, the change in liquid would be in the neighborhood of 100 mL per feeding session. If the cross-sectional area of the bin is small enough, the change in distance would be quite noticeable. What do you think based on this new information that I have missed out earlier?

  6. #21
    user_88 Newbie
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    If your number .... 100 mL .... or 100 cubic centimeters .... per actuation ...is correct, then the ultrasonic T/R might not be the best choice. A graduated cylinder, or anything of such a small dimension might have peripheral interference from the container walls ....The idea is to detect a distinct echo pulse from the fluid surface .......
    A larger diameter cross sectional area would be better....have more of a chance of working properly. ...Apparently there is a dispersion of the ultrasonic wave from the transmitter ..... at some acute angle.

    If you were to place a transmitter at some point above a 1 cm diameter cylinder, not within it, and generate a pulse, it may be that there would not be sufficient energy in the reflected wave to be picked up by the ultrasonic receiver.

  7. #22
    user_88 Newbie
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    Quote Originally Posted by ssylee View Post
    This is more like an industrial project for research purposes. The solution needs to be able to withstand quite caustic environments, aka ammonia. In terms of accuracy, the change in liquid would be in the neighborhood of 100 mL per feeding session. If the cross-sectional area of the bin is small enough, the change in distance would be quite noticeable. What do you think based on this new information that I have missed out earlier?
    It may be that you want to find a means to determine the height of the fluid column by measuring the pressure at the lowest point .... the base of the fluid column. The pressure of a fluid column is equal to:
    (fluid density) * (g ... a gravitational constant) * (height)
    or P=ρgH.
    The great thing here is that there are a wide variety of pressure sensors to choose from. You should be able to find one that will have enough 'resolution' .... smallest measurement interval ... to be able to detect the 100 mL increments that you anticipate. You will have to decide what form you want the data to take .... Voltage A/D conversion .... or whatever, but that should be a trivial problem.

    n.b. : technically, the first sensor parameter that you will want to consider is the 'resolution' or the smallest increment that can be measured.
    The term 'accuracy' is related to the consistency of repeated measurements.

  8. #23
    Roff Excellent Roff Excellent Roff Excellent Roff Excellent Roff Excellent Roff Excellent Roff Excellent Roff Excellent Roff Excellent Roff Excellent
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    I just realized that ssylee has hijacked mersenne31's thread. I wonder what happened to him?
    Ron


  9. #24
    ssylee Newbie
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    Quote Originally Posted by user_88 View Post
    It may be that you want to find a means to determine the height of the fluid column by measuring the pressure at the lowest point .... the base of the fluid column. The pressure of a fluid column is equal to:
    (fluid density) * (g ... a gravitational constant) * (height)
    or P=ρgH.
    The great thing here is that there are a wide variety of pressure sensors to choose from. You should be able to find one that will have enough 'resolution' .... smallest measurement interval ... to be able to detect the 100 mL increments that you anticipate. You will have to decide what form you want the data to take .... Voltage A/D conversion .... or whatever, but that should be a trivial problem.

    n.b. : technically, the first sensor parameter that you will want to consider is the 'resolution' or the smallest increment that can be measured.
    The term 'accuracy' is related to the consistency of repeated measurements.
    Sorry for getting "accuracy" and "resolution" mixed up. For accuracy, of course I would want the system to be as consistent as possible. For the resolution, the change in liquid could go anywhere between 20 mL to 200 mL, but for operational purposes, the smallest liquid mass change should be about 10 mL.

  10. #25
    user_88 Newbie
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    Quote Originally Posted by ssylee View Post
    Sorry for getting "accuracy" and "resolution" mixed up. For accuracy, of course I would want the system to be as consistent as possible. For the resolution, the change in liquid could go anywhere between 20 mL to 200 mL, but for operational purposes, the smallest liquid mass change should be about 10 mL.
    Just as an initial approximation...say you have a cylindrical container of
    1 cm diameter, and using water as the fluid of interest:
    Then a 10 mL change in the volume of the container would equal about 10 cm of vertical height change. The pressure change due to this same height change would be in the neighborhood of 1 kN, or 0.01 bar, or 0.15 lb/sq. in., or equivalently, about 4 in. of water.
    This would be the approximate resolution to look for in a pressure transducer.
    ....just using water in the column.

    Do you have a value for the density of the liquid that will be used?

  11. #26
    ssylee Newbie
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    The density of the liquid is remarkably close to water, so assuming that it's water would be fine. Are you suggesting a pressure sensor to sense the pressure change due to the change in the amount of liquid? The container used is around 150 L, while the bin is around 25 cm high, so the cross-sectional area is quite large.

  12. #27
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    Quote Originally Posted by ssylee View Post
    The density of the liquid is remarkably close to water, so assuming that it's water would be fine. Are you suggesting a pressure sensor to sense the pressure change due to the change in the amount of liquid? The container used is around 150 L, while the bin is around 25 cm high, so the cross-sectional area is quite large.
    ... Given this information, the question is: what will the change in vertical height of liquid in the bin be, if the minimum liquid volume amount is removed from the container?

    I am guessing that the minimum Δh of the fluid will not be a very great quantity.

    Consequently, the ΔP of the fluid at the bottom of the container will hardly change at all...

    So, the pressure sensor method is not likely to work.

    .... Going back to the ultrasonic transducer, I have doubts about using any sort of home made / microcontroller unit, due to the lack of resolution....
    As I recall, the home brew version could only measure to within a few centimeters ....Maybe a commercial ultrasonic level meter could give the desired results for your application.... would cost more though.

  13. #28
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    Default Peristaltic Pump

    There is a type of low flow rate pump that works by repetitive squeezing of a flexible tube. The tubing comes in various types .... depending on what chemical resistance is required. You would have to set up some sort of counter mechanism to measure amount of fluid delivered ... and some way to turn the pump on and off... Not sure about the economics ....
    Welcome: TAT Pumps Peristaltic Pump Manufacuring and Sales

  14. #29
    ssylee Newbie
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    I actually got some new information about the apparatus. Even though the tank is 150 L, the ideal flow rate is actually around 1 to 2 L/min. So the change in liquid volume would be much larger than I thought. Given the new information, I guess the change in liquid level would be much more significant that ultrasound may fit as a suitable solution now. The current apparatus uses a pump to pump the liquid out, with the time that the pump is on translates into the amount of liquid consumed.

  15. #30
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    Quote Originally Posted by ssylee View Post
    I actually got some new information about the apparatus. Even though the tank is 150 L, the ideal flow rate is actually around 1 to 2 L/min. So the change in liquid volume would be much larger than I thought. Given the new information, I guess the change in liquid level would be much more significant that ultrasound may fit as a suitable solution now. The current apparatus uses a pump to pump the liquid out, with the time that the pump is on translates into the amount of liquid consumed.
    To use either the ultrasonic or the pressure method, you have to have a significant change in the height of the fluid level. Even a Δh resulting from 1 or 2 liter effluent from the container may not be sufficient for these methods to work...If your value of 25 cm for the container wall height is correct, then for 150 L of fluid, you would have about 0.6 m˛ of container area....quite a large area, considering the height of the container wall.

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