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Introduction to Acoustics

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Method 2<br />

Alternatively, over the temperature range 0–30 ◦ C, with<br />

a computation [24.72–74] that is based on the derivation<br />

of real-gas sound speed from virial coefficients, the<br />

dry-air sound speed c0 calculated with 16 coefficients<br />

similar <strong>to</strong> those shown in Table 24.8, is 331.46 m/s.<br />

The uncertainty is approximately 545 ppm [24.73, 74],<br />

which encompasses sound speeds c0 from 331.279 <strong>to</strong><br />

331.641 m/s. It should be noted that the sound speed of<br />

331.29 m/s obtained with the first method is within the<br />

uncertainty range of the second method [24.50].<br />

Within the normal range of environmental conditions<br />

during calibration, the following simplified<br />

equation [24.38, 40, 50] for the sound speed in humid<br />

air may be used:<br />

� �1/2 T<br />

c = c0 (1 + 0.165hs)∆, (24.B4)<br />

T0<br />

where hs is the fractional molar concentration of moisture,<br />

and ∆ is a fac<strong>to</strong>r <strong>to</strong> compensate for dispersion.<br />

Values of ∆ = 0.99935 and ∆ = 0.99965 are found<br />

in [24.81] and [24.82], respectively. A value of 1.0001<br />

has also been obtained [24.72].<br />

Over a frequency range of 10 Hz <strong>to</strong> 10 kHz, by ignoring<br />

the dispersion fac<strong>to</strong>r ∆, the uncertainty in the<br />

sound speeds obtained with methods 1 and 2 increases<br />

by approximately 300 ppm.<br />

By ignoring dispersion, at the reference conditions<br />

of 23 ◦ C, 101.325 kPa and 50% relative humidity, the<br />

sound speed obtained with (24.B4) is 196 ppm higher<br />

than that obtained with (24.B3).<br />

24.B.3 Ratio of Specific Heats of Air<br />

There have been several experimental [24.83, 84] and<br />

theoretical [24.71–74,85,86] investigations in<strong>to</strong> the variation<br />

of the ratio of specific heats of air with temperature,<br />

humidity, pressure and carbon dioxide content [24.75]<br />

([24.86], pp. 36–39). A general empirical equation has<br />

been obtained [24.71] for the calculation of the variation<br />

of γ/γ0 with relative humidity h, temperature t and<br />

carbon dioxide content hc<br />

γ/γ0 = a0 + a1t + a2t 2 + a3hc + a4hct + a5hct 2<br />

+ a6h + a7ht + a8ht 2 + a9ht 3 + a10(hc) 2<br />

+ a11h 2 + a12hthc , (24.B5)<br />

where a0–a12 are coefficient constants listed in Table<br />

24.8. With (24.B5), the above normalized ratio of<br />

specific heats can be deduced by multiplying γ/γ0 by<br />

the corresponding reference dry-air ratio of specific<br />

Microphones and Their Calibration 24.B Physical Properties of Air 1047<br />

heats γ0. ForCO2 content hc values from 0% <strong>to</strong> 1%,<br />

and for temperatures of 0–30 ◦ C, humidity from 0 <strong>to</strong><br />

1 (relative humidity 0% <strong>to</strong> 100%), and at a barometric<br />

pressure of 101.325 kPa, the ratio of specific heats computed<br />

using the numerical coefficients in Table 24.8,<br />

fit the theoretical data with a standard uncertainty of<br />

±17 ppm.<br />

Uncertainties in γ0<br />

Based on method 1 above [24.71], the dry-air specific<br />

heat ratio γ0 is 1.3998. The standard uncertainty in γ0 is<br />

approximately 400 ppm.<br />

Similarly, based on method 2 [24.72–74], the dry-air<br />

specific heat ratio γ0 is 1.4029; the standard uncertainty<br />

in γ0 is over 760 ppm.<br />

24.B.4 Viscosity and Thermal Diffusivity<br />

of Air for Capillary Correction<br />

The viscosity η of air, in the parameters in (24.39)<br />

of Sect. 24.4.3, is a function of temperature t. Anempirical<br />

equation which is based on a least-squares fit <strong>to</strong><br />

published data [24.87]is<br />

η =[17.26797 + (5.0756 × 10 −2 )t<br />

− (4.4028 × 10 −5 )t 2 + (5.0000 × 10 −8 )t 3 ]<br />

×10 −6 Pa s (24.B6)<br />

The equation for the thermal diffusivity αt of<br />

air [24.38, 40]is<br />

αt = η(9κ − 5)/(4κρ)m 2 /s . (24.B7)<br />

Uncertainties in η<br />

Over the temperature range from −80 ◦ C <strong>to</strong> 100 ◦ C,<br />

when compared with the published data [24.87], the<br />

maximum deviation in η obtained with (24.B6) is<br />

±1 ppm from the data points. However, the data point<br />

uncertainty may be several percent [24.87].<br />

For standard dry air at a pressure of 101.325 kPa,<br />

the numerical values calculated with the above equations<br />

for the viscosity are 1.7268 × 10 −5 Pa s and<br />

1.8413 × 10 −5 Pa s, at 0 and 23 ◦ C, respectively; and<br />

the corresponding values for the thermal diffusivity<br />

are 1.812 34 × 10 −5 m 2 /sand2.095 49 × 10 −5 m 2 /s,<br />

respectively.<br />

Examples. Aiming at the highest accuracies (method 1),<br />

Table 24.9 gives the recommended values of the<br />

quantities given in (24.B2)–(24.B4) for the reference<br />

Part H 24.B

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