This solution details the calculation of the void fraction ($\epsilon$) for a packed bed bioreactor using the given flow rate and velocity data.
Convert the volumetric flow rate ($Q$) from litres per second (L/s) to cubic centimeters per second (cm3/s) for consistency:
$Q = 0.025 \frac{\text{L}}{\text{s}} \times \frac{1000 \text{ cm}^3}{1 \text{ L}} = 25 \text{ cm}^3 \text{ s}^{-1}$
Calculate the total cross-sectional area ($A$) of the packed bed using the inside diameter ($D$):
$A = \frac{\pi D^2}{4}$
$A = \frac{\pi (10 \text{ cm})^2}{4} = \frac{100\pi}{4} \text{ cm}^2 = 25\pi \text{ cm}^2$
The superficial velocity ($v_s$) is the average velocity of the fluid based on the total reactor cross-sectional area. It is calculated as:
$v_s = \frac{Q}{A}$
$v_s = \frac{25 \text{ cm}^3 \text{ s}^{-1}}{25\pi \text{ cm}^2} = \frac{1}{\pi} \text{ cm s}^{-1}$
The relationship between interstitial velocity ($v_i$), superficial velocity ($v_s$), and void fraction ($\epsilon$) is given by $v_i = \frac{v_s}{\epsilon}$. Therefore, the void fraction is:
$\epsilon = \frac{v_s}{v_i}$
Substitute the values:
$\epsilon = \frac{1/\pi \text{ cm s}^{-1}}{1 \text{ cm s}^{-1}} = \frac{1}{\pi}$
Calculating the numerical value:
$\epsilon \approx 0.318309...$
Rounding the void fraction to two decimal places:
$\epsilon \approx 0.32$