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Small Systems Which Approach Complete Homogenization Solution for such a case is assumed to be of the form C(x,t) = X(x) T(t) ----- (1) [Note: Solutions.

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Presentation on theme: "Small Systems Which Approach Complete Homogenization Solution for such a case is assumed to be of the form C(x,t) = X(x) T(t) ----- (1) [Note: Solutions."— Presentation transcript:

1 Small Systems Which Approach Complete Homogenization Solution for such a case is assumed to be of the form C(x,t) = X(x) T(t) ----- (1) [Note: Solutions for infinite systems were of the form C(x,t) = f(x/  t)] Substituting equation in Fick’s second law equation, we get Only way this equation can be true is if both L.H.S and R.H.S. of the equation are equal to a constant. In addition, the constant must be negative, for the inhomogeneities to disappear with time.

2  T =T 0 exp ( - 2 Dt)  X= A’ Sin x + B’ Cos x A n, B n, and n are obtained from the boundary conditions. A n example of a problem involving small systems is diffusion out of a slab.

3 Diffusion Out of a Slab Boundary conditions: For 0<x<h, C = C o t = 0 For x=0 and x= h, C = 0 at t>0 and C = C o at t=0 C=0 at x=0,t >0  B n =0 C=0 at x=h, t>0  Sin n x = Sin n h = 0  n h = n   n = (n  /h)

4 C = Co at t = 0 for 0 < x < h  Multiply both sides by Sin (p  x/h) and integrate from 0 to h. All the terms in the integral on the R.H.S. with n  p are zero. With n=p,

5 A n = 0 for all even n for all odd n So A n can be written in terms of an integer variable “j” instead of ‘n’ as follows

6 Each successive term is smaller than the preceding one. For longer times, h 2 <16 Dt, one can consider only the first term. Average concentration in the slab is given by, For longer times,

7 Homogenization At x = 0, l, 2l, 3l, … Flow occurs from regions of –ve curvature to regions with +ve curvature.

8 At t=0, where the relaxation time,  = (l 2 /  2 D B ) Amplitude  decreases exponentially with time. Longer the , longer the homogenization process.

9 Thin Film Solution In the previous two cases dealing with infinite systems, we had infinite sources of solute. We assumed that the interface concentration remains constant. When we had a fixed amount of solute at the interface to diffuse out to the adjacent regions, the form of the solution is different. For a case where a fixed amount of solute  kg/m 2 (or other appropriate units)) is placed at the interface between two long rods with initial concentration of 0, the solution is given by The total quantity of solute is conserved 


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