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Maleic anhydride is to be hydrolysed in three stirred tank reactors in series. When H₂O is in excess, the reaction rate can be considered as pseudo-first order with respect to the anhydride concentration, k = 0.2570 s1. Each reactor has a volume of 2500 cm³. The temperature is constant and the feed rate to the first reactor is 682 cm³ s-1. Calculate the conversion accomplished in each of the three reactors if the initial concentration of maleic anhydride is 2.5 mol L-¹.

Maleic anhydride is to be hydrolysed in three stirred tank reactors in series. When H₂O is in excess, the reaction rate can be considered as pseudo-first order with respect to the anhydride concentration, k = 0.2570 s1. Each reactor has a volume of 2500 cm³. The temperature is constant and the feed rate to the first reactor is 682 cm³ s-1. Calculate the conversion accomplished in each of the three reactors if the initial concentration of maleic anhydride is 2.5 mol L-¹.

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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Maleic anhydride is to be hydrolysed in three stirred tank reactors in series. When H₂O is in excess, the reaction rate can be considered as pseudo-first order with respect to the anhydride concentration, k = 0.2570 s1. Each reactor has a volume of 2500 cm³. The temperature is constant and the feed rate to the first reactor is 682 cm³ s-1. Calculate the conversion accomplished in each of the three reactors if the initial concentration of maleic anhydride is 2.5 mol L-¹.
Transcribed Image Text:Maleic anhydride is to be hydrolysed in three stirred tank reactors in series. When H₂O is in excess, the reaction rate can be considered as pseudo-first order with respect to the anhydride concentration, k = 0.2570 s1. Each reactor has a volume of 2500 cm³. The temperature is constant and the feed rate to the first reactor is 682 cm³ s-1. Calculate the conversion accomplished in each of the three reactors if the initial concentration of maleic anhydride is 2.5 mol L-¹.
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