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An exothermic, aqueous phase, irreversible, first order reaction, Y Z is carried out in an ideal continuous stirred tank reacto (CSTR) operated adiabatically at steady state. Rate of consumption of Y (in mol liter"minute) is given by 6500 -1; = 10°e TC; Where C, is the concentration of Y (in mol liter), and T is the temperature of the reaction mixture (in K). Reactant Y is fed a 50°C. Its inlet concentration is 1.0 mol literand its volumetric flow rate is 1.0 liter minute. In addition, use the following data and assumptions Heat of the reaction = -42000 Jmol" • Specific heat capacity of the reaction mixture = 4.2 g K • Density of the reaction mixture = 10000 g liter Heat of the reaction, specific heat capacity and density of the reaction mixture do no vary with temperature Shaft work is negligible If the conversion of Y at the exit of the reactor is 90 %, the volume of the CSTR (in liter) is (round off to 2 decimal places)

An exothermic, aqueous phase, irreversible, first order reaction, Y Z is carried out in an ideal continuous stirred tank reacto (CSTR) operated adiabatically at steady state. Rate of consumption of Y (in mol liter"minute) is given by 6500 -1; = 10°e TC; Where C, is the concentration of Y (in mol liter), and T is the temperature of the reaction mixture (in K). Reactant Y is fed a 50°C. Its inlet concentration is 1.0 mol literand its volumetric flow rate is 1.0 liter minute. In addition, use the following data and assumptions Heat of the reaction = -42000 Jmol" • Specific heat capacity of the reaction mixture = 4.2 g K • Density of the reaction mixture = 10000 g liter Heat of the reaction, specific heat capacity and density of the reaction mixture do no vary with temperature Shaft work is negligible If the conversion of Y at the exit of the reactor is 90 %, the volume of the CSTR (in liter) is (round off to 2 decimal places)

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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An exothermic, aqueous phase, irreversible, first order reaction, Y → Z is carried out in an ideal continuous stirred tank reactor (CSTR) operated adiabatically at steady state. Rate of consumption of Y (in mol liter"minute¯') is given by 6500 |-1; =10°2T Where C, is the concentration of Y (in mol liter"'), and T is the temperature of the reaction mixture (in K). Reactant Y is fed at C- 50°C. Its inlet concentration is 1.0 mol liter¯,and its volumetric flow rate is 1.0 liter m inute. In addition, use the following data and assumptions Heat of the reaction = -42000 Jmol Specific heat capacity of the reaction mixture = 4.2 g¯K Density of the reaction mixture = 10000 g liter Heat of the reaction, specific heat capacity and density of the reaction mixture do no vary with temperature Shaft work is negligible If the conversion of Y at the exit of the reactor is 90 %, the volume of the CSTR (in liter) is (round off to 2 decimal places).
Transcribed Image Text:An exothermic, aqueous phase, irreversible, first order reaction, Y → Z is carried out in an ideal continuous stirred tank reactor (CSTR) operated adiabatically at steady state. Rate of consumption of Y (in mol liter"minute¯') is given by 6500 |-1; =10°2T Where C, is the concentration of Y (in mol liter"'), and T is the temperature of the reaction mixture (in K). Reactant Y is fed at C- 50°C. Its inlet concentration is 1.0 mol liter¯,and its volumetric flow rate is 1.0 liter m inute. In addition, use the following data and assumptions Heat of the reaction = -42000 Jmol Specific heat capacity of the reaction mixture = 4.2 g¯K Density of the reaction mixture = 10000 g liter Heat of the reaction, specific heat capacity and density of the reaction mixture do no vary with temperature Shaft work is negligible If the conversion of Y at the exit of the reactor is 90 %, the volume of the CSTR (in liter) is (round off to 2 decimal places).
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