ENGR266 Summer 2018 Q A3[PARTIAL] official answers Left out: Parts (c) (5 marks, fugacity of a pure gas from $Z(P)$ via $\ln\phi = \int_0^P (Z-1)\,dP/P$), (d) (2 marks, definition of the excess Gibbs energy) and (e) (8 marks, excess Gibbs energy of benzene/water from modified Raoult's law activity coefficients and Antoine equations) are left out: fugacity, excess Gibbs energy and activity coefficients are not in the current slides or formula sheets (audit tag CHECK).
Answer ALL parts (a) - (e)
Formulas you may need
- Phase rule: (two-phase binary at fixed : one degree of freedom, so each fixes and ) (on the formula sheet)
- Reading a P-x-y diagram: bubble point from the bubble (liquid, ) curve, the coexisting vapour from the dew () curve at the same (tie line) (learn this)
- (a)[6]ThirdPlot the following vapour liquid equilibrium data for the acetone(1) / methanol(2) mixture on the graph paper provided and add labels to show the liquid and vapour regions and indicate which lines correspond to the bubble and dew curves.
Pressure /kPa 17 0.0 0.0 20 0.22 23 0.21 0.38 27 0.46 0.59 30 0.77 0.81 31 1 1 - (b(i))[2]The acetone(1) / methanol(2) binary mixture contains a mole fraction of acetone of 0.3. (i) What is the mole fraction of acetone in the first bubble that is formed when the pressure crosses the bubble curve.
- (b(ii))[2](ii) What is the mole fraction of acetone in the first droplet that is formed when the pressure crosses the dew curve.