A liquid mixture of benzene and toluene is to be separated in a continuous
single-stage equilibrium flash tank. The pressure in the unit may be adjusted
to any desired value, and the heat input may similarly be adjusted to vary the
temperature at which the separation is conducted. The vapor and liquid product
streams both emerge at the temperature \(T\left(^{\circ} \mathrm{C}\right)\) and
pressure \(P(\mathrm{mm} \mathrm{Hg})\) maintained in the vessel. Assume that
the vapor pressures of benzene and toluene are given by the Antoine equation,
Table B.4 or APEx; that Raoult's law- -Equation 6.4-1 - applies; and that the
enthalpies of benzene and toluene liquid and vapor are linear functions of
temperature. Specific enthalpies at two temperagiven here for each substance
in each phase. \(\mathrm{C}_{6} \mathrm{H}_{6}(\mathrm{l})
\quad\left(T=0^{\circ} \mathrm{C}, \quad \hat{H}=0 \mathrm{kJ} /
\mathrm{mol}\right) \quad\left(T=80^{\circ} \mathrm{C}, \quad \hat{H}=10.85
\mathrm{kJ} / \mathrm{mol}\right)\)
\(\mathrm{C}_{6} \mathrm{H}_{6}(\mathrm{v}) \quad\left(T=80^{\circ} \mathrm{C},
\hat{H}=41.61 \mathrm{kJ} / \mathrm{mol}\right) \quad\left(T=120^{\circ}
\mathrm{C}, \hat{H}=45.79 \mathrm{kJ} / \mathrm{mol}\right)\)
\(\mathrm{C}_{7} \mathrm{H}_{8}(\mathrm{l}) \quad\left(T=0^{\circ} \mathrm{C},
\quad \hat{H}=0 \mathrm{kJ} / \mathrm{mol}\right) \quad\left(T=111^{\circ}
\mathrm{C}, \hat{H}=18.58 \mathrm{kJ} / \mathrm{mol}\right)\)
\(\mathrm{C}_{7} \mathrm{H}_{8}(\mathrm{v}) \quad\left(T=89^{\circ} \mathrm{C},
\hat{H}=49.18 \mathrm{kJ} / \mathrm{mol}\right) \quad\left(T=111^{\circ}
\mathrm{C}, \hat{H}=52.05 \mathrm{kJ} / \mathrm{mol}\right)\) (a) Suppose the
feed is equimolar in benzene and toluene \(\left(z_{\mathrm{B}}=0.500\right) .\)
Take a basis of 1 mol of feed and do the degree-of-freedom analysis on the
unit to show that if \(T\) and \(P\) are specified, you can calculate the molar
compositions of each phase \(\left(x_{\mathrm{B}} \text { and }
y_{\mathrm{B}}\right),\) the moles of the liquid and vapor products
\(\left(n_{\mathrm{L}} \text { and } n_{\mathrm{V}}\right),\) and the required
heat input \((Q) .\) Don't do any numerical calculations in this part. (b) Do
the calculations of Part (a) for \(T=90^{\circ} \mathrm{C}\) and \(P=652
\mathrm{mm} \mathrm{Hg}\). (c) For \(z_{B}=0.5\) and \(T=90^{\circ} \mathrm{C},\)
there is a range of feasible operating pressures for the evaporator, \(P_{\min
}
P_{\max } ?[\)
Hint: Look at your solution to Part (b) and think about how it would change
if you lowered \(P .]\) (d) Set up a spreadsheet to perform the calculation of
Part (b) and then use it to determine \(P_{\max }\) and
\(P_{\text {min. }}\) The spreadsheet should appear as follows (some solutions
are shown): Additional columns may be used to store other calculated variables
(e.g., specific enthalpies). Briefly explain why \(Q\) is positive when \(P=652
\mathrm{mm}\) Hg and negative when \(P=714 \mathrm{mm} \mathrm{Hg}\).
(e) In successive rows, repeat the calculation for the same \(z_{\mathrm{B}}\)
and \(T\) at several pressures between \(P_{\min }\) and \(P_{\text {max. Generate
a plot }}\) (using the spreadsheet program itself, if possible) of
\(n_{\mathrm{V}}\) versus \(P . \mathrm{At}\) approximately what pressure is half
of the feed stream vaporized?
Jets of high-speed steam are used in spray cleaning. Steam at 15.0 bar with
\(150^{\circ} \mathrm{C}\) of superheat is fed to a well-insulated valve at a
rate of \(1.00 \mathrm{kg} / \mathrm{s}\). As the steam passes through the
valve, its pressure drops to 1.0 bar. The outlet stream may be totally vapor
or a mixture of vapor and liquid. Kinetic and potential energy changes may be
neglected.
(a) Draw and label a flowchart, assuming that both liquid and vapor emerge
from the valve. (b) Write an energy balance and use it to determine the total
rate of flow of enthalpy in the outlet stream \(\left(\dot{H}_{\text {out
}}=\dot{m}_{1} \hat{H}_{1}+\dot{m}_{v} \hat{H}_{v}\right) .\) Then determine
whether the outlet stream is in fact a mixture of liquid and vapor or whether
it is pure vapor. Explain your reasoning. (c) What is the temperature of the
outlet stream?
(d) Assuming that your answers to Parts (b) and (c) are correct and that the
pipes at the inlet and outlet of the valve have the same inner diameter, would
\(\Delta E_{\mathrm{k}}\) across the valve be positive, negative, or explain.