I'm relatively new to HYSYS dynamics, and am having to brush up a great deal on process control in general. My component mole fractions are 0.02 C1, 0.43 C2, 0.3 C3, 0.125 iC4, 0.125 nC4. The feed enters a fractionation column where C2 is the LK. I am using a feed valve and PI flow controller...