(B) The gas phase reaction A 3C is carried out in a flow reactor with no pressure drop. Pure A enters at a temperature of 400 K and a pressure of 10 atm. At this temperature, Kc = 0.25 (mol/d³)². (3) Calculate the equilibrium conversion and concentration when the gas phase reaction is carried out in a constant-volume batch reactor. (4) Calculate the equilibrium conversion and concentration when the gas phase reaction is carried out in a constant-pressure batch reactor.

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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**Gas Phase Reaction Analysis:**

**Reaction:**
\[ A \rightleftharpoons 3C \]

This reaction is conducted in a flow reactor with no pressure drop. Pure A is introduced at a temperature of 400 K and a pressure of 10 atm. At this temperature:

\[ \text{K}_c = 0.25 \, (\text{mol/d}^3)^2 \]

**Objectives:**

1. **Constant-Volume Batch Reactor:**
   - Calculate the equilibrium conversion and concentration when the reaction is carried out in a constant-volume batch reactor.

2. **Constant-Pressure Batch Reactor:**
   - Calculate the equilibrium conversion and concentration when the reaction is carried out in a constant-pressure batch reactor.
Transcribed Image Text:**Gas Phase Reaction Analysis:** **Reaction:** \[ A \rightleftharpoons 3C \] This reaction is conducted in a flow reactor with no pressure drop. Pure A is introduced at a temperature of 400 K and a pressure of 10 atm. At this temperature: \[ \text{K}_c = 0.25 \, (\text{mol/d}^3)^2 \] **Objectives:** 1. **Constant-Volume Batch Reactor:** - Calculate the equilibrium conversion and concentration when the reaction is carried out in a constant-volume batch reactor. 2. **Constant-Pressure Batch Reactor:** - Calculate the equilibrium conversion and concentration when the reaction is carried out in a constant-pressure batch reactor.
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