CHEMICAL ENGINEERING Two bulbs are connected by a straight tube, 0.001 m in diameter and 0.15 m in length. Initially the bulb at end 1 contains N2 and the bulb at end 2 contains H2. The pressure and temperature are maintained constant at 25°C and 1 atm. At a certain time after allowing diffusion to occur between the two bulbs, the nitrogen content of the gas at end 1 of the tube is 80 mol% and at end 2 is 25 mol%. If the binary diffusion coefficient is 0.784 cm2 /s, determine: (a) The rates and directions of mass transfer of hydrogen and nitrogen in mol/s (b) The species velocities relative to stationary coordinates, in cm/s
Let A = N2, B= H2
T = 273 + 25 = 298 K
P = 1 atm = 101325 Pa
Since P, T are kept constant we can assume equimolar counterdiffusion of A & B
PA1 = 101325 * 80 /100 = 81060 Pa, PA2 = 101325 * 25 /100 = 25331.25 Pa
PB1 = 101325 * 20 /100 = 20265 Pa, PB2 = 101325 * 75 /100 = 75993.75 Pa
Na = - (0.784 x 10-4 m2/s) (PA2 - PA1 Pa) / (8.314 J/mol-K * 298 K * 0.15 m)
= 0.012 mol/m2-s
Nb = - Na = -0.012 mol/m2-s
A = pi*d2/4 = 3.14 * 0.0012 / 4 = 7.85 x 10-7 m2
Ra = Na. A = 0.012 * 7.85 x 10-7 = 9.23 x 10-9 mol/s
Rb = -9.23 x 10-9 mol/s (B diffuses in opposite direction)
Mole density = P / RT = n/V (mol/m3)
Mole density (Rho) = 101325 / (8.314 * 298) = 40.9 mol/m3
Volumetric Flow = Ra/Rho = 9.23 x 10-9 / 40.9 = 2.26 x 10-10 m3/s
Species velocity of A = Vol. Flow / A = 2.26 x 10-10 / 7.85 x10-7 = 2.9 x 10-4 m/s
Species velocity of B = - 2.9 x 10-4 m/s
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