Referring to the figure below, what volume of the titrant was used to reach half-neutralization equivalence point?141210864210 20 30 4о50 60Volume of 0.1000 M HCI, mLFigure 8-4 Curve for the titration of 25.00 mL of 0.1000 M Na,CO, with 0.1000 M HCI.(A20 mLB50 mL25 mL56 mLHd

Given that v1 =25 mlMNa2CO3=0.1 MMHCl =0.1M

Answered: Referring to the figure below, what…

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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Draw a T-xy diagram to combine the two components water and ethanol at one atmosphere pressure
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You must base your solutions for this problem on vapor pressure correlations in the form of Antoine's Equation In psat 1 mm Hg with the following parameter values: Compound i benzene toluene Ethylbenzene n-propylbenzene n-butylbenzene A₁ 15.9008 16.0137 16.0195 16.0062 16.0793 B₁ A₁ T+ Cu T+C₁ B₁ 2788.51 3096.52 3279.47 3433.84 3633.40 G₁ -52.36 -53.67 -59.95 -66.01 -71.77 T is in Kelvin and Pat is in mm Hg. Note that more data is given than needed to solve the problem. (As is often the case when looking up data...) a) Calculate and plot the Txy phase diagram for vapor-liquid equilibria of binary mixtures of benzene (light) and ethylbenzene (heavy) at atmospheric pressure. Assume validity of Raoult's law. b) Use your results from part a) to plot the xy equilibrium curve for vapor-liquid equilibria of binary mixtures of benzene and ethylbenzene at atmospheric pressure. Remember that the plots are to use mole fraction of the lighter component as their axes. Banzane *

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Referring to the figure below, what volume of the titrant was used to reach half-neutralization equivalence point? 14 12 10 2 на