Any help on how to set this up would be great.

0.3177 0.5894 0.0715 0.0214 1.0000 Effect of EOS on Calculations Hydrogen (H) Methane (M) In the thermal hydrodealkylation of toluene to benzene Benzene (B) Toluene (T) (C2H + H2 CH + CH4), excess hydrogen minimizes cracking of aromatics to light gases. In practice, conversion of toluene per pass through the reactor is only 70%. To separate and recycle hydrogen, hot reactor effluent vapor of 5,597 kmol/h at 500 psia (3,448 kPa) and 275 F (408.2 K) is partially condensed to 120 F (322 K), with phases separated in a flash drum. If the composition of the reactor effluent is as given above and the flash pressure is 485 psia (3,344 kPa), calculate equilibrium compositions and flow rates of vapor and liquid leaving the drum and the amount of heat transferred, using a process simulation program for each of the equation-of-state models discussed above. Compare the results, including K-values and enthalpy and entropy changes