1. An industry uses a stirred tank reactor to carry out a homogeneous liquid phase reaction. First into the reactor dissolved in solution A (in air) containing 0.05 gmol A/L. At the start of the reaction, the reactor was run continuously in a new solution A of 0.15 gmol/L at a rate of 21 solutions/min. The results were taken continuously at the same speed of 2L solution/minute. The reaction that occurs is a first order reaction with a reaction rate constant at a reaction temperature of k = 0.1 minutes. The reactor volume available is 10 L. A. Calculate the concentration of A in the solution leaving the reactor after the reaction has been running for 3 minutes B. Calculate the concentration of A in the solution leaving the reactor after the steady-state is reached
1. An industry uses a stirred tank reactor to carry out a homogeneous liquid phase reaction. First into the reactor dissolved in solution A (in air) containing 0.05 gmol A/L. At the start of the reaction, the reactor was run continuously in a new solution A of 0.15 gmol/L at a rate of 21 solutions/min. The results were taken continuously at the same speed of 2L solution/minute. The reaction that occurs is a first order reaction with a reaction rate constant at a reaction temperature of k = 0.1 minutes. The reactor volume available is 10 L. A. Calculate the concentration of A in the solution leaving the reactor after the reaction has been running for 3 minutes B. Calculate the concentration of A in the solution leaving the reactor after the steady-state is reached
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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