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An elementary irreversible liquid-phase reaction, 2A→B, is carried out under isothermal conditions in a 1 m³ ideal plug flow reactor (PFR) as shown in the figure. The volumetric flow rate of fresh A, v₁ = 10 m³ h-1, and its concentration CA₁ = 2 kmol m³. For a recycle ratio R = 0, the conversion of A at location 2 with respect to the fresh feed (location 1) is 50%. For R→∞, the corresponding conversion of A is % (rounded off to one decimal place). Fresh feed 1 m³ v₁ = 10 m³ h-1 VR CA1 = 2 kmol m³ PFR R = VRV₂ 2

An elementary irreversible liquid-phase reaction, 2A→B, is carried out under isothermal conditions in a 1 m³ ideal plug flow reactor (PFR) as shown in the figure. The volumetric flow rate of fresh A, v₁ = 10 m³ h-1, and its concentration CA₁ = 2 kmol m³. For a recycle ratio R = 0, the conversion of A at location 2 with respect to the fresh feed (location 1) is 50%. For R→∞, the corresponding conversion of A is % (rounded off to one decimal place). Fresh feed 1 m³ v₁ = 10 m³ h-1 VR CA1 = 2 kmol m³ PFR R = VRV₂ 2

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 elementary irreversible liquid-phase reaction, 2A→ B, is carried out under isothermal conditions in a 1 m³ ideal plug flow reactor (PFR) as shown in the figure. The volumetric flow rate of fresh A, v, = 10 m3 h-1, and its concentration CI = 2 kmol m-3. For a recycle ratio R = 0, the conversion of A at location 2 with respect to the fresh feed (location 1) is 50%. For R → 00, the corresponding conversion of A is, to one decimal place). _% (rounded off Fresh feed 1 m3 v, = 10 m h-1 CA1 = 2 kmol m3 PFR R= VV2
Transcribed Image Text:An elementary irreversible liquid-phase reaction, 2A→ B, is carried out under isothermal conditions in a 1 m³ ideal plug flow reactor (PFR) as shown in the figure. The volumetric flow rate of fresh A, v, = 10 m3 h-1, and its concentration CI = 2 kmol m-3. For a recycle ratio R = 0, the conversion of A at location 2 with respect to the fresh feed (location 1) is 50%. For R → 00, the corresponding conversion of A is, to one decimal place). _% (rounded off Fresh feed 1 m3 v, = 10 m h-1 CA1 = 2 kmol m3 PFR R= VV2
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