Question 27.3: Recall the drug capsule described in Example 2. The present ...
Recall the drug capsule described in Example 2. The present drug capsule consists of a 0.652-cmdiameter spherical bead (radius of 0.326 \mathrm{~cm} ) containing a uniform initial concentration of 68.9 \mathrm{mg} / \mathrm{cm}^{3} dramamine. (a) what is the residual concentration of dramamine at the center of the spherical bead after 48 \mathrm{~h} ? (b) the capsule is now a cube 0.652 \mathrm{~cm} on a side. Recalculate part (a) above. (c) the capsule is now a cylindrical tablet of diameter 0.652 \mathrm{~cm} and thickness 0.3 \mathrm{~cm}. Recalculate part (a) above. The diffusion coefficient of dramamine (species A ) in the gel matrix (species B ) is 3 \times 10^{-7} \mathrm{~cm}^{2} / \mathrm{s} at a body temperature of 37^{\circ} \mathrm{C}. The three capsules are presented in Figure 27.7.

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This problem is readily solved using the charts given in Appendix F.
(a) Spherical capsule: First, calculate the relative time \left(X_{D}\right), relative position (n), and relative resistance (m) based on the spherical coordinate system
\begin{gathered} X_{D}=\frac{D_{A B} t}{R^{2}}=\frac{\left(3 \times 10^{-7} \frac{\mathrm{cm}^{2}}{\mathrm{~s}}\right)\left(48 \mathrm{~h} \frac{3600 \mathrm{~s}}{1 \mathrm{~h}}\right)}{(0.326 \mathrm{~cm})^{2}}=0.488 \\ n=\frac{r}{R}=\frac{0 \mathrm{~cm}}{0.326 \mathrm{~cm}}=0(\text { center of sphere }) \\ m=\frac{D_{A B}}{k_{c} R} \approx 0 \end{gathered}
From Figure F.1 or Figure 18.3, the value for Y, which in this case is the unaccomplished concentration change at the center of the spherical bead, is about 0.018. We can now calculate c_{A}
Y=0.018=\frac{c_{A s}-c_{A}}{c_{A s}-c_{A o}}=\frac{0-c_{A}}{0-68.9 \mathrm{mg} / \mathrm{cm}^{3}}
The residual Dramamine concentration at the center of the bead after 48 \mathrm{~h}\left(c_{A}\right) is 1.24 \mathrm{mg} / \mathrm{cm}^{3}.
(b) For the cube-shaped capsule the distance from the midpoint of the cube to any of the six faces is 0.652 \mathrm{~cm} / 2. The relative time X_{D} is now defined as
X_{D}=\frac{D_{A B} t}{x_{1}^{2}}=\frac{\left(3 \times 10^{-7} \frac{\mathrm{cm}^{2}}{\mathrm{~s}}\right)\left(48 \mathrm{~h} \frac{3600 \mathrm{~s}}{1 \mathrm{~h}}\right)}{(0.326 \mathrm{~cm})^{2}}=0.488
Values for n and m are unchanged, with n=0 and m=0. As all of the faces of the cube are of equal dimension, let
Y=Y_{a} Y_{b} Y_{c}=Y_{a}^{3}
From the appendix Figure F.4, given X_{D}=0.488, \mathrm{~m}=0 and n=0, Y_{a} is 0.4 for a flat plate of semi-thickness x_{1}=a=0.326 \mathrm{~cm}. Extending this value to a three-dimensional cube using the above relationship, we have
Y=Y_{a}^{3}=(0.4)^{3}=0.064
Finally,
Y=0.064=\frac{c_{A s}-c_{A}}{c_{A s}-c_{A o}}=\frac{0-c_{A}}{0-68.9 \mathrm{mg} / \mathrm{cm}^{3}}
with c_{A}=4.41 \mathrm{mg} / \mathrm{cm}^{3} after 48 \mathrm{~h}.
(c) For a cylindrical capsule with exposed ends, R=0.652 \mathrm{~cm} / 2 for the radial coordinate, and x_{1}=a=0.3 \mathrm{~cm} / 2 for the axial coordinate. The relative times are
X_{D}=\frac{D_{A B} t}{R^{2}}=\frac{\left(3.0 \times 10^{-7} \frac{\mathrm{cm}^{2}}{\mathrm{~s}}\right)\left(48 \mathrm{~h} \frac{3600 \mathrm{~s}}{1 \mathrm{~h}}\right)}{(0.326 \mathrm{~cm})^{2}}=0.488
for the cylindrical dimension and
X_{D}=\frac{D_{A B} t}{x_{1}^{2}}=\frac{\left(3.0 \times 10^{-7} \frac{\mathrm{cm}^{2}}{\mathrm{~s}}\right)\left(48 \mathrm{~h} \frac{3600 \mathrm{~s}}{1 \mathrm{~h}}\right)}{(0.15 \mathrm{~cm})^{2}}=2.30
for the axial dimension. Values for n and m are unchanged, with n=0 and m=0. From Figures F.1 and F.2, respectively, Y_{\text {cylinder }}=0.1 for the cylindrical dimension and Y_{a}= 0.006 for the axial dimension. Therefore,
Y=Y_{\text {cylinder }} Y_{a}=(0.1)(0.006)=0.0006
and finally
Y=0.006=\frac{c_{A s}-c_{A}}{c_{A s}-c_{A o}}=\frac{0-c_{A}}{0-68.9 \mathrm{mg} / \mathrm{cm}^{3}}
with c_{A}=0.413 \mathrm{mg} / \mathrm{cm}^{3} after 48 \mathrm{~h}. As Y_{a} \ll Y_{\text {cylinder }}, the flux directed out of the exposed ends of the cylindrical tablet along the axial dimension dominates.
The above calculations assume that convective mass-transfer resistances associated with external fluid flow over the surface of the capsule are negligible. Problems in Chapter 30 will reconsider the drug release for unsteady-state diffusion and convection in series.



