P3-16 Calculate the equilibrium conversion and concentrations for each of the fol- lowing reactions. (a) The liquid-phase reaction A + B — с with Cao Cao = 2 mol/dm³ and Kc = 10 dm³/mol. (b) The gas-phase reaction A 3C carried out in a flow reactor with no pressure drop. Pure A enters at a tem- perature of 400 K and 10 atm. At this temperature, K = 0.25idm/mol). (c) The gas-phase reaction in part (b) carried out in a constant-volume batch reactor. (d) The gas-phase reaction in part (b) carried out in a constant-pressure batch
P3-16 Calculate the equilibrium conversion and concentrations for each of the fol- lowing reactions. (a) The liquid-phase reaction A + B — с with Cao Cao = 2 mol/dm³ and Kc = 10 dm³/mol. (b) The gas-phase reaction A 3C carried out in a flow reactor with no pressure drop. Pure A enters at a tem- perature of 400 K and 10 atm. At this temperature, K = 0.25idm/mol). (c) The gas-phase reaction in part (b) carried out in a constant-volume batch reactor. (d) The gas-phase reaction in part (b) carried out in a constant-pressure batch
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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Transcribed Image Text:system and (2) a constant volume bateh system!
P3-16 Calculate the equilibrium conversion and concentrations for each of the fol-
lowing reactions.
(a) The liquid-phase reaction
A + B — с
with CAO = CO 2 mol/dm³ and Kc
(b) The gas-phase reaction
= 10 dm³/mol.
A
30
carried out in a flow reactor with no pressure drop. Pure A enters at a tem-
perature of 400 K and 10 atm. At this temperature, K = 0.25idm³/moljª.
(c) The gas-phase reaction in part (b) carried out in a constant-volume batch
reactor.
(d) The gas-phase reaction in part (b) carried out in a constant-pressure batch
reaction.
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