ENGR263 2023 Q A2(a)-(b)Past paperOld spec ENGR2632:116 marks19 min

ENGR263 Process Transfer of Mass Summer 2023 (open book) Q A2[PARTIAL] official answers Left out: (c) (9 marks), McCabe-Thiele design of a continuous distillation column, is distillation and off-syllabus.

Answer ALL parts (a) - (c). [Part (c), a McCabe-Thiele distillation design (9 marks), is omitted.]

Formulas you may need
  • Diffusion through a stagnant gas: NA=DABPRT(z2−z1)ln⁡P−pA2P−pA1N_A = \dfrac{D_{AB}P}{RT(z_2 - z_1)}\ln\dfrac{P - p_{A2}}{P - p_{A1}} (on the formula sheet)
  • Multicomponent stagnant mixture 1DA,mix=∑j≠Ayj′DAj\dfrac{1}{D_{A,mix}} = \sum_{j \ne A}\dfrac{y'_j}{D_{Aj}}, yj′y'_j on an A-free basis (on the formula sheet)
  • R=82.06 cm3 atm mol−1 K−1=8314 J kmol−1 K−1R = 82.06\ \mathrm{cm^3\,atm\,mol^{-1}\,K^{-1}} = 8314\ \mathrm{J\,kmol^{-1}\,K^{-1}} (learn this)
  1. (a)
    Water is held at the bottom of a narrow metal tube at a constant temperature of 318 K. The dry ambient air outside the tube is at 1 atm and 318 K. Water evaporates and diffuses through the air in the tube, and the diffusion path z2−z1z_2 - z_1 is 30 cm long (from the water surface at z1z_1 to the open top at z2z_2). Calculate the rate of evaporation at steady state in mol/(s cm2)\mathrm{mol/(s\,cm^2)}. The diffusivity of water vapour (A) in air (B) at 1 atm and 318 K is 0.282 cm2/s0.282\ \mathrm{cm^2/s}. Vapour pressure of water at 318 K is 9.5 kPa. Assume that air is insoluble in water.
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  2. (b)
    At 298 K and total pressure of 1 atm, methane (A) is diffusing at a steady state through non-diffusing argon (B) and helium (C). At position z1=0z_1 = 0, the partial pressures of the gases (in atm) are pA1=0.4p_{A1} = 0.4, pB1=0.4p_{B1} = 0.4 and pC1=0.2p_{C1} = 0.2, and at position z2=0.005z_2 = 0.005 m, pA2=0.1p_{A2} = 0.1, pB2=0.6p_{B2} = 0.6 and pC2=0.3p_{C2} = 0.3. The binary diffusivities are DAB=2.02×10−5 m2/sD_{AB} = 2.02 \times 10^{-5}\ \mathrm{m^2/s}, DAC=6.75×10−5 m2/sD_{AC} = 6.75 \times 10^{-5}\ \mathrm{m^2/s} and DBC=7.29×10−5 m2/sD_{BC} = 7.29 \times 10^{-5}\ \mathrm{m^2/s}. Calculate the flux of methane NAN_A (kmol/(m2 s)\mathrm{kmol/(m^2\,s)}).
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