Pressure-temperature graph without zero y-intercept

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A high school physics teacher conducted an experiment measuring the pressure of air in a boiling tube using a manometer filled with water, but found that the pressure-temperature graph did not intersect at zero as expected. The teacher calculated absolute pressure by adding local atmospheric pressure to the relative pressure derived from the manometer readings. Concerns were raised about the impact of gas volume changes and temperature measurement accuracy on the results, particularly since the thermometer in the boiling tube responded slowly compared to the water bath thermometer. The teacher's experimental gradient was significantly lower than theoretical calculations, leading to confusion about the discrepancies. Suggestions included using a mercury-filled manometer instead of water to avoid measuring the pressure of air saturated with water vapor.
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I am a high school physics teacher and I've been trying out an experiment for my students. I used a manometer (a plastic tube in a U-shape partially filled with water) to measure the pressure of the air in a boiling tube. I placed the boiling tube into a beaker of water and varied the temperature. I recorded the head difference in mm and converted this to metres.

I used (pressure = density of water x 9.81 x head) to work out the pressure (relative to atmospheric pressure). I then added the local atmospheric pressure (sourced from BBC Weather in millibars and converted to Pa) to the relative pressure to get the absolute pressure of the air.

I plotted a graph of temperature (in Kelvin) against absolute pressure (in Pa) and got a nice straight line relationship. However, my y-intercept should be at zero, according to the ideal gas laws, but is actually crossing at around 90,000 Pa.

Either my gradient is much too shallow (my points are very close to the line of best fit) or I have an absolute error that has shifted my results up the y-axis. The most likely source of this is the atmospheric pressure.

I'm very puzzled and have probably made a silly error somewhere. If you're interested in checking my numbers, please have a look at the attached spreadsheet.

Thanks,

Rob
 

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Did you use some large gas reservoir in the experiment?
If your gas is in the tube only, the moving water level will change its volume significantly, together with its temperature.
 
mfb said:
Did you use some large gas reservoir in the experiment?
If your gas is in the tube only, the moving water level will change its volume significantly, together with its temperature.

That is something that concerned me, although I would expect a changing volume to cause the line to curve.

The temperature measurement may also be a source of error. I did have a thermometer in the boiling tube, but decided instead to use the one in the water bath. This was because the gas appeared to expand almost immediately (and settle) after the boiling tube was placed in the bath, whereas the thermometer in the boiling tube responded very slowly. This would suggest to me that the rate of heat transfer was much faster through the wall of the boiling tube than it was between the warmed air and the thermometer, so the thermometer in the water bath was more representative of the air temperature than the thermometer in the boiling tube.
 
although I would expect a changing volume to cause the line to curve.
Not significantly, if the volume change is the dominating effect.
Assuming a constant width of the pipe, I get a nice match if the air has a height of 1500mm above your zero-point.
 
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mfb said:
Assuming a constant width of the pipe, I get a nice match if the air has a height of 1500mm above your zero-point.

What do you mean by this?

I've done some calculations of the theoretical pressure (pV=nRT) and get a gradient of 346 (as opposed to 42 for the experimental results). I've also built into my calculations an allowance for the change in volume of the air within the manometer - this changes the gradient to 228.

I'm just very perplexed by how far off these results are. I used a boiling tube as the gas reservoir. I've estimated the volume of boiling tube and pipework to be about 64ml, with the changing volume in the manometer being no more than around 3ml. Significant, but it shouldn't dominate.

I've attached my updated calculations (including theoretical pressure) and a photo of the equipment I used.

Any ideas would be greatly appreciated!
 

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If the manometer is filled with water then you are not measuring the pressure of air but the pressure of air saturated with water vapour.
You should be using a mercury filled manometer.
 
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