In order to obtain a reasonable level of conversion at a commercially acceptable rate, ammonia synthesis reactors operate at pressures of 150 to 300 atm and temperatures of 700 to 750 K. Calculate the equilibrium mole fraction of dinitrogen at 300 atm and 723 K starting from an initial composition of XN2 = 0.25, XH2= 0.75 (Xi is the mole fraction of species i). At 300 atm and 723 K, the equilibrium constant, Ka , is 6.6 X 10^- 3
In order to obtain a reasonable level of conversion at a commercially acceptable rate, ammonia synthesis reactors operate at pressures of 150 to 300 atm and temperatures of 700 to 750 K. Calculate the equilibrium mole fraction of dinitrogen at 300 atm and 723 K starting from an initial composition of XN2 = 0.25, XH2= 0.75 (Xi is the mole fraction of species i). At 300 atm and 723 K, the equilibrium constant, Ka , is 6.6 X 10^- 3
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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In order to obtain a reasonable level of conversion at a commercially acceptable rate, ammonia synthesis reactors operate at pressures of 150 to 300 atm and temperatures of 700 to
750 K. Calculate the equilibrium mole fraction of dinitrogen at 300 atm and 723 K starting
from an initial composition of XN2 = 0.25, XH2= 0.75 (Xi is the mole fraction of species i).
At 300 atm and 723 K, the equilibrium constant, Ka , is 6.6 X 10^- 3
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