The parap was prowided by the manufacturer along with a chanacterisec mamp curve. We wish to use this curve to determine the resulting operating mass fllowrate of liquid benzene. Assume in the process that all benzene up to the inlet of the beat exchanger is at 20C all benzene after the outlet of the beat exchanger is at 80C, and as as approximatioe, assume all benzene in the heat exchanger has a density and viscosity that are the averages of what they are at 200C and 80C. Inside the heat exchanger, the total piping leagth is 3.25m, but that includes two 180 bends that each have values of c=0.55. The pump curve is given below, and you bave curve-litted the data getting the following expression: H=1501.2789103Q2 where AH is in meters, and Q is in L/ min. all your work, and fill in and include the following table: \begin{tabular}{|c|c|c|} \hline & Value & units \\ \hline Hin & & m \\ \hline Hout & & m \\ \hlineHpump & & m \\ \hline Hloss & & m \\ \hline Qcold & & L/min \\ \hline Qhot & & L/min \\ \hline w & & kg/min \\ \hline vcold & & m/s \\ \hline Vhot & & m/s \\ \hline Recold & & -- \\ \hlineRRehot & & -- \\ \hline fcold & & -- \\ \hline fhot & & -- \\ \hline \end{tabular}