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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 в • 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 ° Cin the condenser and the saturated steam flow at 6 bar pressure in the reboiler.

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 в • 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 ° Cin the condenser and the saturated steam flow at 6 bar pressure in the reboiler.

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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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.
Transcribed Image 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.
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