- Consider A Nonideal Binary Gas Mixture With The Simple Equation Of State V Pnrt Nb A The Rule Of Lewis And Randall St 1 (92.46 KiB) Viewed 47 times
Consider a nonideal binary gas mixture with the simple equation of state V=pnRT+nB (a) The rule of Lewis and Randall st
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Consider a nonideal binary gas mixture with the simple equation of state V=pnRT+nB (a) The rule of Lewis and Randall st
Consider a nonideal binary gas mixture with the simple equation of state V=pnRT+nB (a) The rule of Lewis and Randall states that the value of the mixed second virial coefficient BAB is the average of BAA and BBB. Show that when this rule holds, the fugacity coefficient of A in a binary gas mixture of any composition is given by lnϕA=BAAp/RT By comparing this expression with lnϕ≈RTBp for a pure gas, express the fugacity of A in the mixture as a function of the fugacity of pure A at the same temperature and pressure as the mixture. (b) The rule of Lewis and Randall is not accurately obeyed when constituents A and B are chemically dissimilar. For example, at 298.15 K, the second virial coefficients of H2O(A) and N2( B) are BAA=−1158 cm3 mol−1 and BBB=−5 cm3 mol−1, respectively, whereas the mixed second virial coefficient is BAB=−40 cm3 mol−1. When liquid water is equilibrated with nitrogen at 298.15 K and 1bar, the partial pressure of H2O in the gas phase is pA=0.03185 bar. Use the given values of BAA,BBB, and BAB to calculate the fugacity of the gaseous H2O in this binary mixture. Compare this fugacity with the fugacity calculated with the value of BAB predicted by the rule of Lewis and Randall.