In constant-rate filtration, the flow rate is constant: \[ \frac{V}{t} = \text{constant} \] Given: \[ V_1 = 120,\; t_1 = 1\ \text{min} \] \[ V_2 = 240,\; t_2 = 2\ \text{min} \] Thus, \[ \frac{V_1}{t_1} = \frac{V_2}{t_2} \] Cake resistance is proportional to cake mass, which is proportional to filtrate volume: \[ R_c \propto V \] At constant rate, pressure drop must increase proportionally to cake resistance: \[ \frac{\Delta P_2}{\Delta P_1} = \frac{R_{c2}}{R_{c1}} = \frac{V_2}{V_1} \] \[ \Delta P_2 = 10\ \text{kPa} \times \frac{240}{120} = 20\ \text{kPa} \]
