For the HDA process, 1. Calculate the mixing temperature after combining the toluene feed (Stream 1) and the recycled toluene (Stream 11) in V-101 to get Stream 2, which is leaving pump P-101 to the next part of the process. Compare your results (flowrate, composition and temperature with that reported in the textbook for Stream 2. H101 101 W101 P.IS E-101 Tone Food Fedon Fond Puma Peter T. 11 Podem Congo V. High 104 105 Rullu Pame Product Coder FG Temperature (C) Per Mase Flow (1000 combustion products T-101 Bone R-101 V-102 W01 -101 C-1013 V-104 CHO 5-105 Hydrogen 5-100 P.101A/B 5-106 -102B -101 V-100 De TDANO Benzone via the Hydration of Toluene Figure 1.5 Benzene Process How Diagram (PED) for the Production of Bennene via the Hydrodicallylation of Toluene 2 Table 1.5 Flow Summary Table for the Benzese Process Shown in Figure 1.3 (and Figure 1.5) Table 1.5: Flow summary Table for HAD process (continues Stream Number 9 10 11 12 13 14 15 16 1 Temperature 25 995 226 4140041 654 e 112 112 112 >>> Prense (har) 1.90 258 25 22 25 25.0 285 Vapor Fraction 240 33 25 0.0 0.0 1.00 10 33 25 10 23 10 10 10 10 00 0.0 00 20 00 00 10.0 10 Mice Flow Conne/h) 1 133 2015 20.5 0:36 116 Mole Flow mol/h) 14.0 227 1089 821 261 O 1442 301.0 12044 758.8 12014 1100.5 1200 102 35 1056 3042 ComponentMol Flow 4 (mmol/l) Hydroge 00 0.0 2860 735.4 4494 735.4 252 6510 0.00 . Methane 00 170 0.0 0.0 00 15.0 9173 2002 3193 16.95 00 Bene 00 00 12306 0.0 00 76 66 0:37 Toluene 1160 1063 11 IN) 2 1052 1083 1402 25 0 0.0 1410 07 1440 00 LOS 150 16 ON 1.22 122 04 31 Do 10 75 o m' (TH-46) ya PP PSUM Pati yTyBole fraction 1516 012518 3.209731 bar In (pp)A-BXTC) T PP TO B THT 120 155 ha m' B T 'Cp 225-Tb) T CPs AH-integ (Cp dT) 0- m'p (225-46) BAT m'. AHCpi TIK H2 CH4 TO 40 313 2 654 01211925 2.925121 In cpp)A-BTC PP TO 2 & CH 13 38 Q E-102