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.2.1 1. 1. 2-I 3..4. 5--6 7- 8..9- I - 10.- 11. 12- 13. 14- -15. 16 17. 18. I II. The adiabatic exothermic irreversible gas-phase reaction 2A + B→ 20 is to be carried out in a flow reactor for an equimolar feed of A and B. A Levenspiel plot for this reaction is shown in the figure: 500,000 400,000 300,000 Fe (m) -TA 200,000 100,000 0.3 0.6 0.9 1. What PFR volume is necessary to achieve 50% conversion? 2. What CSTR volume is necessary to achieve 50% conversion? 3. What is the volume of a second CSTR added in series to the first CSTR (Part b) necessary to achieve an overall conversion of 80%? 4. What PFR volume must be added to the first CSTR (Part b) to raise the conversion to 80%? 5. What conversion can be achieved in a 6 x 10ʻ m² CSTR? In a 6 x 10ʻ m³ PFR?

.2.1 1. 1. 2-I 3..4. 5--6 7- 8..9- I - 10.- 11. 12- 13. 14- -15. 16 17. 18. I II. The adiabatic exothermic irreversible gas-phase reaction 2A + B→ 20 is to be carried out in a flow reactor for an equimolar feed of A and B. A Levenspiel plot for this reaction is shown in the figure: 500,000 400,000 300,000 Fe (m) -TA 200,000 100,000 0.3 0.6 0.9 1. What PFR volume is necessary to achieve 50% conversion? 2. What CSTR volume is necessary to achieve 50% conversion? 3. What is the volume of a second CSTR added in series to the first CSTR (Part b) necessary to achieve an overall conversion of 80%? 4. What PFR volume must be added to the first CSTR (Part b) to raise the conversion to 80%? 5. What conversion can be achieved in a 6 x 10ʻ m² CSTR? In a 6 x 10ʻ m³ PFR?

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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AutoSave Document1 - Word O Search (Alt+Q) ff RICAMAE SALADAGA RS File Home Insert Draw Design Layout References Mailings Review View Help P Comments B Share X Cut O Find v Calibri (Body) - A A Aa v A AаBЬСcDd AaBbСcDd AaBbC AаBЬСc[ Аа B АавьссD v 11 LE Copy Replace Paste BIUV ab x, x A . I v A - I Normal 1 No Spac. Heading 1 Heading 2 Title Subtitle Dictate Sensitivity Editor Reuse S Format Painter A Select v Files Clipboard Font Paragraph Styles Editing Voice Sensitivity Editor Reuse Files |· 2: 1 1 |· ·1: 3.1. 4 5.. 6 . I 7.1· 8.I 10.1 11.| 12:1 13. 14. I 15. 16 17.1 18 | 19 II. The adiabatic exothermic irreversible gas-phase reaction 2A + B → 20 is to be carried out in a flow reactor for an equimolar feed of A and B. A Levenspiel plot for this reaction is shown in the figure: 500,000 400,000 300,000 FAO -rA 200,000 100,000 0.3 0.6 0.9 1. What PFR volume is necessary to achieve 50% conversion? 2. What CSTR volume is necessary to achieve 50% conversion? 3. What is the volume of a second CSTR added in series to the first CSTR 12 (Part b) necessary to achieve an overall conversion of 80%? 4. What PFR volume must be added to the first CSTR (Part b) to raise the conversion to 80%? 5. What conversion can be achieved in a 6 x 104 m³ CSTR? In a 6 x 104 m³ PFR? Page 1 of 1 O words English (Philippines) * Accessibility: Investigate D. Focus 99% 1:10 am O Type here to search W 26°C Mostly clear A a 1 4) ENG 26/02/2022 . 1 · 2 · 1 · 1· I: . . 1· r
Transcribed Image Text:AutoSave Document1 - Word O Search (Alt+Q) ff RICAMAE SALADAGA RS File Home Insert Draw Design Layout References Mailings Review View Help P Comments B Share X Cut O Find v Calibri (Body) - A A Aa v A AаBЬСcDd AaBbСcDd AaBbC AаBЬСc[ Аа B АавьссD v 11 LE Copy Replace Paste BIUV ab x, x A . I v A - I Normal 1 No Spac. Heading 1 Heading 2 Title Subtitle Dictate Sensitivity Editor Reuse S Format Painter A Select v Files Clipboard Font Paragraph Styles Editing Voice Sensitivity Editor Reuse Files |· 2: 1 1 |· ·1: 3.1. 4 5.. 6 . I 7.1· 8.I 10.1 11.| 12:1 13. 14. I 15. 16 17.1 18 | 19 II. The adiabatic exothermic irreversible gas-phase reaction 2A + B → 20 is to be carried out in a flow reactor for an equimolar feed of A and B. A Levenspiel plot for this reaction is shown in the figure: 500,000 400,000 300,000 FAO -rA 200,000 100,000 0.3 0.6 0.9 1. What PFR volume is necessary to achieve 50% conversion? 2. What CSTR volume is necessary to achieve 50% conversion? 3. What is the volume of a second CSTR added in series to the first CSTR 12 (Part b) necessary to achieve an overall conversion of 80%? 4. What PFR volume must be added to the first CSTR (Part b) to raise the conversion to 80%? 5. What conversion can be achieved in a 6 x 104 m³ CSTR? In a 6 x 104 m³ PFR? Page 1 of 1 O words English (Philippines) * Accessibility: Investigate D. Focus 99% 1:10 am O Type here to search W 26°C Mostly clear A a 1 4) ENG 26/02/2022 . 1 · 2 · 1 · 1· I: . . 1· r
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