For the given ternary phase diagram:OA1 CH,COOH0.20.80.40.6Xw0.60.4a.0.80.21/WaH,0O CHCI,10.20.40.60.8XTa. What is the EXACT composition of point a2?b. What is the maximum amount of (in moles) of pure E that can be addedto a 10 mol mixture at point a2 to maintain a two-phase system?c. How many phases does a mixture of these liquids have?LiquidAmountXTXWХЕ(mol)A150.50.250.250.330.330.8200.33C7.50.10.2d. For the mixture in Problem 5c, what are the composition of thephases? If there are two phases, what are the compositions of thetrichloromethane-rich and water-rich phases?

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Answered: For the given ternary phase diagram:…

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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If 28.5 grams of ammonium chloride react to form 9.1 grams of ammonia, how many grams of hydrogen chloride must simultaneously be formed?
A phase-distribution measurement was made for the PEG 3400–dextran T40–water system at 4oC. The following results give the starting composition and the equilibrium compositions of the two resulting phases, all in wt%.Use the Diamond–Hsu method of (8-93) to compute the values of Ai for dextran and PEG. Use those values to produce a tie line with one end at 11.19 wt% PEG in the top phase.
Calculate the following: Number of atoms in 17.42 g of I2 The number of Ca2+ ions in 11.73g of Ca3(PO4)2
5. Consider a mixture of 2 moles of 1-propanol and 8 moles of water at 1 atm (760 mmHg)(a) What would be the composition (mole fractions) of the liquid and gas phases if the system is maintained in equilibrium at 92.35 °C?(b) ) How many moles would be in each phase? Data on the system 1-propanol and water is presented in Figure 5 and Table VIII of: Murti, P., & Van Winkle, M. (1958). I have attached the table to this questionss
Amount of benzene in Still pot: ABW=W·xwABW=200 mol Can you explain why did you write 200 mol instead of 300 mol because 50% of the benzene has evaporated so the remaining should be 300 mol not 200 mol
Using the provided ternary phase diagram 1. What is the number of phases in this liquid mixture? Liquid Amount || Amount (mol) A || 15 B || 20 C || 7.5 xT || xW || xE 0.5 || 0.25 || 0.25 0.33 ||0.33 || 0.33 0.1 || 0.8 || 0.2 2. What are the phase compositions of the mixtures in Problem 1? What are the trichloromethane-rich and water-rich phases' compositions if there are two phases?
5. With reference to the Cu-Zr binary phase diagram below, answer the following questions: a) What is the maximum amount of copper than can dissolve in aZr at 846°C (by atomic%). Calculate the equivalent weight% at this overall composition (you will need to find the atomic weights of both elements). b) What happens if more copper is added after this solubility limit is reached? c) What is the highest temperature eutectic in this system (temperature and composition)? d) Identify a eutectoid point in this diagram using an arrow. e) What happens to CusZr if it is cooled slowly from 700°C to room temperature?
Focus on Example 8.4-5. Show all of the plotting for the relative humidty and dry-bulb temperature. Use any linear interpolation for the enthalpy deviation.
We are tasked to do iteration in mass and energy balances, wherein we will look for the final temperature. When there are two components, like CO and CO2, do you add their enthalpy out (i.e. 3.376 + 0.557x10-3T - 0.031x105T-2 for CO and 5.457 + 1.045x10-3T - 1.157x105T-2 for CO2) to use for the calculation of Cp, mean? If yes, what would be the value of Cp, mean?
Conversion of cis-2-butene to trans-2-butene is represented by the equation kc=trans/Cisco. Calculate the equilibrium constant when 3mol of the cis-isomer in 8L is heated to 500 Celsius and at equilibrium the trans-ionomer is 2.1mol.
Binary Distillation Water / n-Butanol System. A saturated liquid feed of 500 mol/hr containing 40 mole % water is to be fractionated at 101.325kPa (abs) in order to form a distillate containing 70 mole % water and a bottoms product of 10 mole % water. NOTE: This is actually NOT an ideal solution.use the Raoult’s Law data Assume a distillate reflux ratio (if necessary) of 3:1.a) Calculate the flowrates (mol/hr) of the distillate and bottoms.b) Determine the theoretical number of trays and the feed tray number for the specified operation.c) Determine the minimum reflux ratio, RMIN and the minimum number of theoretical trays at total reflux Vapor Pressure Temperature water n-butanol T (F) T (K) T (C) kPa kPa x y 212.2 373.2 100.1 101.498 51.828 1.000 1.000 215.7 375.2 102.0 108.8 56.080 0.861 0.923 219.2 377.1 104.0 116.6 60.613 0.730 0.839 222.8 379.1 106.0 124.8 65.442 0.607 0.747 226.3 381.1 107.9 133.5 70.582 0.491 0.646 229.9 383.0 109.9 142.7…
At the azeotropic composition, the mixture's bubble point and dew point are ________. a complementary b equal to one c equal to zero d equal

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