AE 3051, Lab #16. Investigation of the Ideal Gas State Equation. By: George P. Burdell. Group E3

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AE 3051, Lab #16 Investigation of the Ideal Gas State Equation By: George P. Burdell Group E3 Summer Semester 000

Abstract The validity of the ideal gas equation of state was experimentally tested for three gases: helium (He), argon (Ar) and nitrogen (N). The experiments were conducted in a fixed volume container over a range of pressures (~30-60 kpa) and temperatures (~95-360 K). Gas temperatures were determined with a type-k thermocouple, and the pressures were measured with a mercury manometer. The measurements for each gas were obtained with a single, fixed gas sample; thus each sample had a constant mass. In agreement with the ideal gas law for these conditions, the density ratio, p/rt, was found to be constant, at least within the ~6% uncertainty of the measurements. The uncertainty in p/rt was primarily a result of the repeatability of the pressure and temperature conditions, which could be improved by more carefully ensuring that steady-state is achieved. 1

Introduction An important relationship often used to relate specific gas properties is the ideal gas equation of state. This report describes experiments intended to investigate the validity of this state equation, which can be written as p RT, where p is the absolute pressure, T is the absolute temperature and R is the specific gas constant. In order to verify the ideal gas state equation, the pressure of a fixed gas sample was measured as it was heated in fixed volume container. Three individual gases: helium (He), nitrogen (N) and argon (Ar), were tested. The temperature and pressure inside the container were measured with a thermocouple and a mercury manometer. In addition, the volume of the container was determined by measuring an equivalent volume of water. Experimental Setup Figure 1 illustrates the experimental apparatus employed in this investigation. The fixedvolume, aluminum test cell is composed of a cylindrical body and two end flanges. There are three connections to the cell: the first connects the cell to a control valve and to the high pressure cylinder containing the test gas; the second connects to another control valve and a vacuum pump; and the third connects the cell to a vertical-type mercury manometer. The test cell tubing attaches to the top of the vertical arm of the manometer, while the mercury bath is open to the atmosphere. Mounted vertically, alongside the manometer, is a ruler, which has a fine scale marked in 1/3 units. The apparatus also includes a digital barometer for measuring the local atmospheric pressure in the room. Electrical-resistance heating tape wrapped around the cell controls the cell s temperature, as well as the temperature of the gas inside. The voltage across the heating tape, and therefore the

current through it, is regulated by a variable transformer. A type-k thermocouple passes through the side of the cell and monitors the temperature of the gas inside. The thermocouple leads connect to a calibrated electronic readout unit that includes an electronic reference junction. In order to ensure that the gas temperature is nearly uniform inside the test cell, the cell is covered with insulation. In addition, there is a stirring mechanism at the bottom of the cell that is magnetically-coupled to a motor outside the cell. Valve p High Pressure Gas Cylinders Vacuum Pump Thermocouple Readout Heating Tape Type-K Thermocouple Magnetic Stirrer Test Cell Mercury Manometer p atm Figure 1. Schematic of the experimental apparatus. In order to measure the volume of the cell, the top flange was removed and the cell was filled with water. The water was then emptied into a 100 ml graduated cylinder. After drying the cell carefully, the flange was replaced and tightened. Then the vacuum pump was turned on for a period of 0 minutes so as to empty the cell of air. For each test gas, the following measurement procedure was employed. First, the cell was evacuated with the vacuum pump to a gauge pressure below 9.7 in. Hg. Then, the cell was pressured to ~1 atm with the test gas (at approximately room temperature). This cycle of filling and evacuating was repeated three more times to ensure the cell s contents were limited to the test gas of interest. Then, the test cell was 3

filled to a pressure below 1 atm, the magnetic stirrer was activated, and the thermocouple readout was monitored until it did not change by more than 0.1C in 10 seconds. With the container at steady-state, the pressure and temperature readings were acquired. Next, the voltage on the heating tape was then increased a small amount, and the pressure and temperature measurements were taken again after the thermocouple readout stabilized. Results and Discussion As noted above, the test cell s volume was ascertained by filling the test cell with water and measuring the water volume with the graduated cylinder. This process was repeated a total of 10 times and the results are shown in Table I. The average of the ten measurements is 83 ml, or equivalently, 83 cm 3. Next, the lab group measured the atmospheric pressure using the digital barometer. The measured pressure was 9.66 in. Hg. Table I. Test cell volume results determined from equivalent volume of water. Sample # Volume (ml) 1 83.0 83.0 3 8.5 4 83.0 5 83.0 6 83.5 7 83.0 8 8.5 9 83.0 10 83.0 Initially, six measurements of cell gauge pressures as a function of temperature were taken for each gas. The results are listed in Table II for all three gases (He, N and Ar). The measured temperatures and pressures can be converted to absolute values using the following conversions: 4

p T K T C 73 Pa p in.hg p in.hg 10135Pa 5. 4mmHg gage atm. () 760mmHg 1in.Hg With the measured atmospheric pressure in the test room, Equation () reduces to: Pa p in.hg p 3386 gage 9. 66 (3) The raw data listed in Table II were converted to absolute values using Equations (1) and (3). They are shown plotted in Figure. For all three gases, the data shown in Figure appear to fall along a single line in p,t space. This agrees with the ideal gas state equation, i.e., p=constantt, which is the equation for a line going through the origin. (1) Table II. Pressures and temperatures for 3 gases in a heated, fixed volume container. Gas T (C) pgage (in. Hg) He 0 4/3 He 9 0 17/3 He 38 0 18/3 He 50 19 30/3 He 65 19 10/3 He 85 18 0/3 N 3 0 31/3 N 8 0 4/3 N 40 0 4/3 N 49 0 6/3 N 63 19 18/3 N 81 19 /3 Ar 0 31/3 Ar 30 0 19/3 Ar 39 0 1/3 Ar 51 19 17/3 Ar 63 19 19/3 Ar 84 19 4/3 5

40 p (kpa) 30 0 10 Ar N He Linear Fit 0 50 300 350 400 T (K) Figure. Absolute pressure dependence on absolute temperature for three fixed density gases. In addition to the data points, the graph also shows a linear data fit that passes through the origin (T=0, p=0). An alternate, and arguably more meaningful way, to compare the results to the ideal gas law is to examine the slope of the line, i.e., p/t, or even better, the ratio p/rt. The required mass specific gas constant R is given by: R R (4) M where R is the universal gas constant (8314 J/kmol K) and M is the molecular weight of the gas (see Table III). The results for p/rt are listed in Table IV, and plotted as a function of temperature in Figure 3. Table III. Molecular weights of the gases measured. Gas M (kg/kmol) He 4 N 8 Ar 40 6

Table IV. Measurements of p/rt; also listed are the average value of the ratio for each gas. Gas T (K) p/rt (kg/m 3 ) He 95 0.049 He 30 0.049 He 311 0.0477 He 33 0.0490 He 338 0.0499 He 358 0.050 He Average 0.049 N 96 0.335 N 301 0.338 N 313 0.347 N 3 0.335 N 336 0.343 N 354 0.34 N Average 0.340 Ar 95 0.480 Ar 303 0.488 Ar 31 0.470 Ar 34 0.509 Ar 336 0.488 Ar 357 0.481 Ar Average 0.486 Figure 3 also includes results from a second set of experiments performed to test the repeatability of the measurements. In these tests, one temperature setting (39 C) for the last test gas (Ar) was repeated six more times (see Table V). The measurement was repeated by changing the cell temperature away from 39C, then returning it, and finally measuring the pressure. This complete cycle was repeated for each measurement. As covered in the Error Analysis Appendix, the estimated uncertainty in the average value of p/rt for the repeated case was ~.5%; this corresponds to an estimated uncertainty of 6.5% for the single measurement Ar cases. These uncertainties are indicated with error bars in Figure 3. 7

p/rt (kg/m 3 ) 0.6 0.4 0. Ar N 0.0 50 300 350 400 T (K) Figure 3. Variation in normalized pressure/temperature ratio for three gases of constant mass in a fixed volume container. Also shown are average values for each data set, and the uncertainty in the Ar data based on the analysis in Error Analysis Appendix. Table V. Repeated values of pressure and temperature for Ar at 39C (31 K), and the calculated average including the corresponding single point from the Table IV data. Repeat pgage (in. Hg) p/rt (kg/m 3 ) 1 0 5/3 0.496 0 4/3 0.498 3 0 /3 0.468 4 19 30/3 0.508 5 19 31/3 0.506 6 0 6/3 0.495 Avg 0.491 Since the gas inside the container is trapped and the container volume is fixed (assuming negligible change in the size of the container due to thermal expansion during heating), the measurements for each gas sample are at the same density. According to the ideal gas state equation, =p/rt. So, we would expect the ratio p/rt to remain constant in our experiment as the gas temperature is changed. This is essentially the behavior displayed in Table IV and Figure 8

3. In addition, the ~6.5% single-point uncertainty determined from the repeated Ar measurements is consistent with the variability of the Ar density results seen in Figure 3. Finally, we note that since all the gases were contained in the same volume, we would expect that the measured p/rt values would scale like the molecular weight of each gas. This is exactly the behavior seen in Figure 4, which shows the average p/rt measurement of each gas (see Table IV) as a function of molecular weight. 0.6 p/rt (kg/m 3 ) 0.4 0. N Ar 0.0 He 0 10 0 30 40 50 Molecular Weight Figure 4. Dependence of the density for the three gases as a function of molecular weight of the test gas compared to the linear behavior expected from the ideal gas law. Supplement Questions With the current measurements, we are not able to find the value for the universal gas constant. Another way to write the ideal gas equation of state is pv mrt. In the current experiments, we measured the pressure, volume and temperature, but not the mass of the gas in the test cell. So, we can not determine R as we have only one equation but two unknowns (m and R). 9

In order to test the remainder of the ideal gas law, one would have to determine the mass of gas trapped inside the cylinder with some independent measurement. One possibility would be to weigh the test cell twice: once with a vacuum inside and once when it is loaded with the test gas. The difference would be the weight of the test gas, which could be converted to mass using the standard value for the gravitational acceleration on Earth. We could then compare this to the mass determined from combining: 1) the p and T measurements, ) the ideal gas law, and 3) the volume of the test cell, i.e., p m V (5) RT However, getting an accurate value with Equation (5) would be a very difficult task. Assuming the ideal gas law is accurate, our density results from this experiment for the heaviest gas, Ar, were approximately 0.49 kg/m 3. Since the volume of the test cell was measured to be 83 cm 3, the mass of the Ar inside the cell was only 41 mg. It would be difficult to measure this small change in the mass of the test cell, which was approximately 000g. In other words, an error of 0.1% in the measurement of the empty test cell would be ~g. To increase the mass of gas to the level of our expected uncertainty in the test cell s mass, the initial pressure in the cell would need to be increased from ~80 kpa (see Figure ) to roughly.4 MPa or almost 350 psi. In addition, it would probably require a stronger and heavier chamber to withstand this high pressure, making the measurement even more difficult. In the current experiment, we kept the density of the gas constant and changed its temperature. An alternate approach would be to use a piston-cylinder arrangement to change the volume and, therefore, the density of the gas and measure the pressure and temperature. The drawback to this approach is that the volume would need to change very rapidly and the 10

temperature measurement would need to be quick enough to prevent errors due to heat exchange with the cylinder walls. In other words, if one were to rapidly compress the gas, its temperature would rise above the temperature of the cylinder walls. Very quickly, however, the gas would start losing heat to the walls and the temperature would drop back towards its original value. Summary and Conclusions This report describes an experiment to verify the ideal gas equation of state for three gases: He, N and Ar. Pressures and temperatures were measured for fixed mass samples in a fixed volume container. Since the density of the sample could not change in the fixed volume container, the ideal gas equation would predict that the ratio p/rt, equal to density for an ideal gas, would be constant. For each test gas sample, the measured density was found to vary by less than ~6% as the temperature of the cell was varied over a range of roughly 95-360 K. Also, the variation appears to be random. In other words, it does not appear to be a function of the pressure and temperature. Based on attempts to repeat a single point, most of the variation in the measurements can be attributed to lack of repeatability in reproducing the pressure (and temperature) conditions. Increased attention to ensuring that the cell had reached steady-state would likely reduce this error. In addition, the results showed that the density of the gas samples varied linearly with the molecular weight of the gas as would be expected from the ideal gas law. Limitations in the apparatus did not allow the mass of each sample to be measured. Therefore, the value of the ideal gas constant, R, could not be determined. Still, the current results are sufficient to validate the ideal gas state equation, at least within the range of pressures and temperatures tested. 11

Appendix: Error Analysis Volume The volume of the test cell was measured 10 times (see Table I). The random uncertainty or precision of the volume measurement, uv,prec, can be estimated from the standard deviation of the repeated volume measurements. From the measured values, this is 0.8 ml. Assuming a normal distribution, the random uncertainty in the measured mean volume within a 95% confidence interval is uv,prec= 0.18 ml (1.960.8ml/10 1/ ). One source of systematic or bias error, uv,bias, in the measurement is the accuracy in the markings on the graduated cylinder. The manufacturer suggests that the accuracy of the cylinder is 0.1% of full scale, i.e., 0.1 ml. This is likely the largest systematic error associated with the cylinder itself. Another source of systematic uncertainty in the measurement is the water left in the test cell after it is emptied into the graduated cylinder. Based on a visual observation, this is estimated to be less than 5 drops (< mm diam.) of water or less than 0.0 ml. This can be neglected compared to the other uncertainties. Thus the combined or total uncertainty in the reported mean volume value, as given by u i i, prec ui, bias u (A.1) is uv =0.0 ml. As a percentage of the average value of the measured volume, u V / V = 0.%. Density The density measurements ( p M / RT ) are affected by errors in measurements of the pressure and temperature, as well as the uncertainty in the purity of the gas in the test cell, which influences the molecular weight M. Since the lab group did not make repeated measurements of 1

the temperature or gas sample, we can only estimate the systematic errors of these two measurements. The manufacturer specifies the accuracy of the thermocouple that we used as better than 0.1 C, i.e., ut,bias =0.1 K. With regard to the gas purity, we can estimate the amount of residual gas (nontest gas) left in the cell by considering the refilling process. Each time the cell was evacuated to a pressure below 9.7 in. Hg gage (~670 Pa) and then filled to 1 atm with test gas, the residual gas was diluted to 0.66% (=670/10135) of the test gas. Since the dilution process was repeated four times, the residual gas should compose less than ~10-9 (1 part per billion) of the gas in the cell during the test. Our worst case error would occur with the presence of air in the He test gas (a heavy gas in the lightest test gas). So the bias error can be estimated from the relationship u M and inserting the appropriate values into Eq. (A.), u M, bias M M, bias actual He, (A.) 110 9 9 10 8.8 4 8.5 10 M He 10 9 M Air M The random uncertainty in the pressure measurement can be estimated from the repeated Ar measurements (Table V). Including the original measurement at 39 C (Table II), the standard deviation of the pressure measurements is 1070 Pa. Again using a 95% confidence interval, we He can estimate the uncertainty in the reported average pressure, up,prec 793 Pa (1.961070Pa/7 1/ ). The primary systematic error in the manometer is the accuracy of the height markings, which is estimated to be 1/3 in. or up,bias = 106 Pa. The total pressure uncertainty, 13

from Equation (A.1), is up= 800 Pa, which is essentially the same as the precision uncertainty in the pressure measurement. We can combine all these errors into a single error in density measurement by using the relation, u ut um u (A.3) p T M p The partial derivatives required in Eq. (A.3) are obtained from the ideal gas state equation, so that u pm RT 1 u T T u T p RT 1 u M M u M 1 u p Inserting the uncertainty values given above for the repeated Ar case, we find M RT p u p u 0.1K 31K.510 40 8 800Pa 3350Pa 4 10 3. 10 6 10.5 10 0.05 Thus, the relative error in the current measurements of density for the repeated Ar case is ~.5%. Clearly, the most significant error is the repeatability of the pressure measurements. For the single (nonrepeated) measurements, we can assume the same measurement rms, in which case the overall uncertainty would be 6.5% (i.e., the random uncertainty assuming only a single measurement). This relative error was used to produce the error bars shown in Figure 3. It agrees with the general repeatability of the density measurements for the Ar case, as well as other gases listed in Table IV. The most likely source of this repeatability error is the amount of time that the 14

lab group waited for the system to come to steady-state. It is likely that the thermocouple measurement of the cell temperature was not representative of the actual gas temperature, because the temperature was not uniform inside the cell. One way to reduce this error would be to wait longer before taking data. 15