Can someone please help me with this problem? Part B, ive been stuggling and cannot figure out how to set the mass balance quation and solve for Q. I would greatly appreciate it please

Raked canolaseed containing Nolters an actor where the seed is brought into contact with a team of pure honest women from the odractor. One stream is a midure of Scandinavent and the other team is "Welles containing 25 solventand. Here, the test and diniy whether hexane solvent is present. We are then enter a drying chamber which the files are gently heated under acom. The solvent in the stakes is completely evaporated: pure solvent vapor exits there with an enthalpy of diy falleciderethe wet takes and dry Flakes have a specific heat of 22 and 20k/kg-K, respectively Wo ory A What are the enthalples of the wet takes and dry Calculate the heat input to the dryer per kg wet les entering the dryer? Hint: set the mass rate of wet fakes entering the dryer 1 This emple of the use of a basis for solving problem Stateley assumptions you used parts Given drger Ctractor 3 1 ed Streams Mw.fac) TCH 1-Flaked canolaseed 41 2- Pure hexane solvent 3-"Wet flakes 257 32 22 70-4 4-Canola oil insolvent 29 5-Pure solvent vapor 6- Dry takes 40 20 20-0 Find: A) Enthalpy of wet & dry flakes B) Calculate Q for dryer 1K Sol'n A) Wet flakes = , H2 = (2.2%7ky:X)* (32*9)x 18 = 70.467/kg, Dry flakes H=CATO H6=(2.0k/kg-x) = (40%) X 7 - 12 = 80 kJ/kg (%* B) Q=MCP (AT) 1x 1%