ENGR263 2023 Q A1Past paperOld spec ENGR2632:125 marks30 min

ENGR263 Process Transfer of Mass Summer 2023 (open book) Q A1[VALID] official answers

Answer ALL parts (a) - (c).

Formulas you may need
  • Wilke-Chang: DAB=7.4×10−8(ΦBMB)1/2TμBVA0.6D_{AB} = \dfrac{7.4 \times 10^{-8}(\Phi_BM_B)^{1/2}T}{\mu_BV_A^{0.6}} (DD in cm2/s\mathrm{cm^2/s}, μB\mu_B in cP, VAV_A in cm3/mol\mathrm{cm^3/mol}) (on the formula sheet)
  • Le Bas molar volume: VA=∑V_A = \sum atomic volumes (learn this)
  • Droplet evaporation time θ=ρArs2RT2MADABPln⁡[(P−pA,b′)/(P−pA,s′)]\theta = \dfrac{\rho_Ar_s^2RT}{2M_AD_{AB}P\ln[(P - p'_{A,b})/(P - p'_{A,s})]} (given in the question)
  • Steady diffusion through a plane solid wall NA=DABcA1−cA2δN_A = D_{AB}\dfrac{c_{A1} - c_{A2}}{\delta} (on the formula sheet)
  • Gas solubility in a solid: cA=S pA22.4 L/molc_A = \dfrac{S\,p_A}{22.4\ \mathrm{L/mol}} with SS in volume (STP) of gas per volume of solid per atm (learn this)
  1. (a)
    Estimate the diffusivity of ethyl alcohol (C2_2H5_5OH) in dilute aqueous solution at 20∘C20^\circ\mathrm{C}. For water as solvent, ΦB=2.26\Phi_B = 2.26; molecular weight of water, MB=18.02M_B = 18.02; viscosity of water, μB=0.001005 kg/(m s)\mu_B = 0.001005\ \mathrm{kg/(m\,s)}; atomic volumes of C, H and O are 14.8, 3.7 and 7.4 cm3/mol\mathrm{cm^3/mol}, respectively.
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  2. (b)
    A water droplet with an initial diameter of 10 mm is suspended in a large volume of air. The air is at a temperature of 26.65∘C26.65^\circ\mathrm{C} and a total pressure of 1 atm. Moisture present in the air exerts a partial pressure of 0.01036 atm. The wet-bulb temperature of the water droplet is 15.55∘C15.55^\circ\mathrm{C}, at which temperature the vapour pressure of water is 0.01743 atm. The diffusivity of water vapour at its average temperature of 21.1∘C21.1^\circ\mathrm{C} has been estimated to be 0.2607 cm2/s0.2607\ \mathrm{cm^2/s}. Calculate the time required for complete evaporation of the water droplet. The time required for evaporation from droplets is estimated from equation A1.1: θ=ρA×rs2×R×T2×MA×DAB×P×ln⁡[P−PA,b′P−PA,s′]\theta = \frac{\rho_A \times r_s^2 \times R \times T}{2 \times M_A \times D_{AB} \times P \times \ln\left[\dfrac{P - P'_{A,b}}{P - P'_{A,s}}\right]} where θ\theta is the time (s) required for the evaporation of a droplet with radius rsr_s (cm); water molecular weight MA=18 g mol−1M_A = 18\ \mathrm{g\,mol^{-1}}, density ρA=1 g/cm3\rho_A = 1\ \mathrm{g/cm^3}; RR the gas constant 8.206×10−5 m3 atm/(K mol)8.206 \times 10^{-5}\ \mathrm{m^3\,atm/(K\,mol)}; PA,b′P'_{A,b} and PA,s′P'_{A,s} are the vapour pressures at the bulk gas phase and the surface of the droplet respectively. Comment on the conditions that can lead to a faster evaporation time. The effect of curvature on the vapour pressure of water and convective effect may be neglected.
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  3. (c)
    Hydrogen gas is diffusing through an unglazed neoprene rubber with a wall thickness of 50 mm at 25∘C25^\circ\mathrm{C} and pressure of 1 atm. The solubility of hydrogen in the rubber has been estimated to be 0.053 cm30.053\ \mathrm{cm^3} (at STP, Vmol=22.4V_{mol} = 22.4 litres at STP) of H2_2 per cm3\mathrm{cm^3} of neoprene. The diffusivity of hydrogen through the rubber wall is 1.8×10−6 cm2/s1.8 \times 10^{-6}\ \mathrm{cm^2/s}. Calculate the mass diffusion rate (g/(m2 s)\mathrm{g/(m^2\,s)}) of hydrogen per square meter of the wall.
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