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By analysing the results of PFR and CSTR performance from Figure 1, recommend the best type of reactor to achieve the highest conversion possible to maximize the yield of glucose and LA as well as to minimize the deposition of humins. Justify your answers by using your knowledge in chemical reaction engineering. 100 80 60 (a) (d) 12 10 (b) (e) 40 10 (c) (f) 50 100 150 200 250 300 0 t/ min 50 100 150 200 250 300 t/ min Figure 1 Data taken in continuous reactors of a single PFR (plots a, b, c) and single CSTR (plots d, e, f) for glucose conversion, HMF carbon yield, and LA carbon yield where 160 °C (•) and 180 °C (); Model prediction for 160 °C and for 180 °C represent by dashed and solid line, respectively. Glucose conversion (%) HMF carbon yield (%) Levulinic acid carbon yield (%) 4, ON 2)

By analysing the results of PFR and CSTR performance from Figure 1, recommend the best type of reactor to achieve the highest conversion possible to maximize the yield of glucose and LA as well as to minimize the deposition of humins. Justify your answers by using your knowledge in chemical reaction engineering. 100 80 60 (a) (d) 12 10 (b) (e) 40 10 (c) (f) 50 100 150 200 250 300 0 t/ min 50 100 150 200 250 300 t/ min Figure 1 Data taken in continuous reactors of a single PFR (plots a, b, c) and single CSTR (plots d, e, f) for glucose conversion, HMF carbon yield, and LA carbon yield where 160 °C (•) and 180 °C (); Model prediction for 160 °C and for 180 °C represent by dashed and solid line, respectively. Glucose conversion (%) HMF carbon yield (%) Levulinic acid carbon yield (%) 4, ON 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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By analysing the results of PFR and CSTR performance from Figure 1, recommend the best type of reactor to achieve the highest conversion possible to maximize the yield of glucose and LA as well as to minimize the deposition of humins. Justify your answers by using your knowledge in chemical reaction engineering. 100 80 60 40 (a) (d) 12 10 (b) (e) 60 50 30 (c) (f) 50 100 150 200 250 300 7/ min 100 150 200 250 300 t/ min 50 Figure 1 Data taken in continuous reactors of a single PFR (plots a, b, c) and single CSTR (plots d, e, f) for glucose conversion, HMF carbon yield, and LA carbon yield where 160 °C (•) and 180 °C (); Model prediction for 160 °C and for 180 °C represent by dashed and solid line, respectively. Levulinic acid carbon yield (%) HMF carbon yield (%) Glucose conversion (%) 20
Transcribed Image Text:By analysing the results of PFR and CSTR performance from Figure 1, recommend the best type of reactor to achieve the highest conversion possible to maximize the yield of glucose and LA as well as to minimize the deposition of humins. Justify your answers by using your knowledge in chemical reaction engineering. 100 80 60 40 (a) (d) 12 10 (b) (e) 60 50 30 (c) (f) 50 100 150 200 250 300 7/ min 100 150 200 250 300 t/ min 50 Figure 1 Data taken in continuous reactors of a single PFR (plots a, b, c) and single CSTR (plots d, e, f) for glucose conversion, HMF carbon yield, and LA carbon yield where 160 °C (•) and 180 °C (); Model prediction for 160 °C and for 180 °C represent by dashed and solid line, respectively. Levulinic acid carbon yield (%) HMF carbon yield (%) Glucose conversion (%) 20
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