Temperature: 367.2 °C P = 1.01 bar Qcond = 1117 kW D Mass fraction of HFCI,: 80 % RR = 8.4 Feed stream (F) • Composition (mass fraction) 80% ZrCl, HFCI, • Temperature: 368.5 °C • Pressure: 1.12 bar •...

Extracted text: Temperature: 367.2 °C P = 1.01 bar Qcond = 1117 kW D Mass fraction of HFCI,: 80 % RR = 8.4 Feed stream (F) • Composition (mass fraction) 80% ZrCl, HFCI, • Temperature: 368.5 °C • Pressure: 1.12 bar • Flow rate: 23405.5 kg/h Temperature: 375.1 °C P = 1.12 bar Qreboler = 1222 kW B • Mass fraction of ZrCl, 98% A) Calculate the number of balance steps and trays required. B) Locate the feed. Consider the equilibrium diagram as shown below. 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 C) Calculate the product flow up and down the tower. D) Calculate the required cold water flow at 10 ° C in the condenser and the saturated steam flow at 6 bar pressure in the reboiler. 1.