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% ZrCI, 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. 1 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.
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% ZrCI, 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. 1 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.
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
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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