ENGR266 2018 Q A3Past paperOld spec ENGR2662:210 marks12 min

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: P+F=C+2P + F = C + 2 (two-phase binary at fixed TT: one degree of freedom, so each PP fixes x1x_1 and y1y_1) (on the formula sheet)
  • Reading a P-x-y diagram: bubble point from the bubble (liquid, x1x_1) curve, the coexisting vapour from the dew (y1y_1) curve at the same PP (tie line) (learn this)
  1. (a)
    Plot 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 /kPax1x_1y1y_1
    170.00.0
    200.22
    230.210.38
    270.460.59
    300.770.81
    3111
    [6]Third
  2. (b(i))
    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.
    [2]
  3. (b(ii))
    (ii) What is the mole fraction of acetone in the first droplet that is formed when the pressure crosses the dew curve.
    [2]