The derivation is shown below:
![solution 2 Consider a control volume of thickness az at a distance a from the interface. A | AB Mole balance of A in the cont](//img.homeworklib.com/questions/0a7ed8c0-94b8-11eb-ae51-df740989d989.png?x-oss-process=image/resize,w_560)
![Substituting expression of I. and ra. 0 - DAB dCAL + DAB dCAL - R, (AZ) LA Divide by az O = DAB dCAL - ACAL - R, CA Id2 12+02](//img.homeworklib.com/questions/0b7e4340-94b8-11eb-b0ad-ad251c0ff6c7.png?x-oss-process=image/resize,w_560)
![Putting in boundary conditions, CA=0 as 2. X. O c +Gole) as 20 W, Sept 2) CA = CAO at 2=0 = CAO CAO - C duplo) Substituting c](//img.homeworklib.com/questions/0cc33c20-94b8-11eb-82f0-65cfe49c0d65.png?x-oss-process=image/resize,w_560)
solution 2 Consider a control volume of thickness az at a distance a from the interface. A | AB Mole balance of A in the control volume, Accumulation - Input-output + generation / consumpution. - # Assumptions a one dimensional diffusion (only 2-direction) - steady state condition (accumulation - 0) given conditions ونعلمك سيك هدم حلمك 3 o = JZ A - Izraz A + Aloz A) A is the cross section area. By Ficks Law of diffusion, Jz = - DAR ACA Flux) dz
Substituting expression of I. and ra. 0 - DAB dCAL + DAB dCAL - R, (AZ) LA Divide by az O = DAB dCAL - ACAL - R, CA Id2 12+02 dz lz) DZ Taking 0 lim 12 0 DAB d²CA - R, CA d22 - d²CA - R, CA = 0 dz? DAB This ODE is of form, dy my =o. The solution of the ODE is given by dua - yln) = C, exp (um n) + Ca exp(-5mx). where c. and ca are constants. Thus, For the governing equation, m = k/ DAB. CA/2) = 6, ep 1 e 2 + z elp |- k z IDAB
Putting in boundary conditions, CA=0 as 2. X. O c +Gole) as 20 W, Sept 2) CA = CAO at 2=0 = CAO CAO - C duplo) Substituting c, and ca ICA(Z) = Caolip(-) NDAB b given R = 7.26 cm? DAB solubility of A = 0.84 gmol/L & CAO = 0.84 god/L CA = 21 of CAO - CA = 2. CAO Too Plugging in values, 2. CA - Cho. exp| -17.26. 2). 100 + - $7.26.2 = ln 10.02) 2= - Info.022 cm 57.26 2 = 1.45 cm -