I am currently working with a dead-end ultrafiltration system with constant flux rate. The schematic of the experimental system used for constant flux experiment is shown in the figure attached. The feed reservoir is open, and the peristaltic pump is set at 10 rpm to have the flow rate equal to 8 mL/min (DI water). The pore size of asymmetric commercial membranes is 100 kDa. Since the flow rate is always and must be constant, the pressure will increase as a function of time if there is a fouling on the membrane.
However, in my case the pressure always becomes constant at certain numbers when filtering an homogenous polymeric solution after around 5 minutes, and therefore, the flux decreases as a function of time due to fouling. It is possible that the pressure in the stirred cell is higher than in the feed which causes a pressure drop across the tube connecting the feed, peristaltic pump, and stirred cell. If that is the case, then the peristaltic pump does not pump 8 mL/min the polymeric solution after 5 minutes pumping.
If someone wants to share some experiences regarding this problem, I would really appreciate it.