Question 6.4: Values of the second and third virial coefficients of nitrog...
Values of the second and third virial coefficients of nitrogen trifluoride are as follows:
B=-94.3 cm ^3 \cdot mol ^{-1} \text { and } C=6740 cm ^6 \cdot mol ^{-2} \text { at } 290 K
B=-87.1 cm ^3 \cdot mol ^{-1} \text { and } C=6430 cm ^6 \cdot mol ^{-2} \text { at } 300 K
B=-80.4 cm ^3 \cdot mol ^{-1} \text { and } C=6090 cm ^6 \cdot mol ^{-2} \text { at } 310 K
Calculate H^R and S^R for nitrogen trifluoride at 300 K and 100 bar:
(a) Using expressions based upon the two-term virial equation.
(b) Using expressions based upon the three-term virial equation.
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(a) Here, we employ Eqs. (6.55) and (6.56) for H_R and S_R, respectively. These require the temperature derivative of the second virial coefficient. For this, we use the values at 290 K and 310 K:
\frac{H^R}{R T}=\frac{P}{R}\left(\frac{B}{T}-\frac{d B}{d T}\right) (6.55)
\frac{S^R}{R}=-\frac{P}{R} \frac{d B}{d T} (6.56)
\frac{d B}{d T} \approx \frac{-80.4+94.3}{20}=0.695 cm ^3 \cdot mol ^{-1} \cdot K ^{-1}
Using this value in Eq. (6.55) gives:
\frac{H^R}{R T}=\frac{P}{R}\left(\frac{B}{T}-\frac{d B}{d T}\right)=\frac{100}{83.14}\left(\frac{-87.1}{300}-0.695\right)=-1.19
from which H^R = −2960 J·mol^−1.
Similarly,
\frac{S^R}{R}=-\frac{P}{R} \frac{d B}{d T}=-\frac{100}{83.14}(0.695)=-0.836
from which S^R=-6.95 J \cdot mol ^{-1} \cdot K ^{-1}
(b) In this case we require the temperature derivatives of both B and C, along with the value of the density of NF_3 at 300 K and 100 bar. Solving the three-term virial coefficient iteratively as described in Ex. (3.8) gives V = 178.0 cm^3·mol^−1, or ρ = 0.00562 mol·cm^3. This corresponds to a compressibility factor of Z = 0.714. Applying the same approach as in part (a) for the temperature derivative of C:
\frac{d C}{d T} \approx \frac{6740-6090}{20}=32.5 cm ^6 \cdot mol ^{-2} \cdot K ^{-1}
With these values, Eqs. (6.62) and (6.63) give:
\frac{H^R}{R T}=T\left[\left(\frac{B}{T}-\frac{d B}{d T}\right) \rho+\left(\frac{C}{T}-\frac{1}{2} \frac{d C}{d T}\right) \rho^2\right] (6.62)
\frac{S^R}{R}=\ln Z-T\left[\left(\frac{B}{T}+\frac{d B}{d T}\right) \rho+\frac{1}{2}\left(\frac{C}{T}+\frac{d C}{d T}\right) \rho^2\right] (6.63)
\frac{H^R}{R T}=300\left[\left(\frac{-87.1}{300}-0.695\right) 0.00562+\left(\frac{6430}{300}-\frac{32.5}{2}\right) 0.00562^2\right]=-1.61
\frac{S^R}{R}=\ln (0.714)-300\left[\left(\frac{-87.1}{300}+0.695\right) 0.00562+\frac{1}{2}\left(\frac{6430}{300}+32.5\right) 0.00562^2\right]=-1.27
from which H^R=-4021 J \cdot mol ^{-1} \text { and } S^R=-10.60 J \cdot mol ^{-1} \cdot K ^{-1}
For comparison, values obtained from data in the NIST Chemistry WebBook are H^R=-3540 J \cdot mol ^{-1} \text { and } S^R=-8.83 J \cdot mol ^{-1} \cdot K ^{-1} . The expression based on the two-term virial equation underestimates these, while the expression based on the three-term virial equation overestimates them. Note that the conditions selected correspond to T_r = 1.28 and P_r = 2.24. These are outside the range where we would expect the two-term virial expansion to work well, and it ppears that adding a third term produces an overcorrection.