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syste P3-16, Calculate the equilibrium conve lowing reactions. (a) The liquid-phase reaction Unistan A with CAO = CO= 2 mol/de (b) The gas-phase reaction carried out in a flow reactor perature of 400 K and 10 ac (c) The gas-phase reaction reactor. (d) The gas-phase reaction reaction.

syste P3-16, Calculate the equilibrium conve lowing reactions. (a) The liquid-phase reaction Unistan A with CAO = CO= 2 mol/de (b) The gas-phase reaction carried out in a flow reactor perature of 400 K and 10 ac (c) The gas-phase reaction reactor. (d) The gas-phase reaction reaction.

Introduction to Chemical Engineering Thermodynamics
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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system and (2) a constant volume batch 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 CA = C0 = 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 = 0.25(dm³/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.
Transcribed Image Text:system and (2) a constant volume batch 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 CA = C0 = 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 = 0.25(dm³/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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