Simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: Optimization using the simplex lattice design

Copyright © 2018 John Wiley & Sons, Ltd. Bio-oil produced via fast pyrolysis of biomass usually has various undesired properties that can negatively affect its use. Therefore, raw bio-oil needs first to undergo an upgrading stage before it is further used. This paper deals with the study of bi...

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Main Authors: Chawannat Jaroenkhasemmeesuk, Maria Elena Diego, Nakorn Tippayawong, Derek B. Ingham, Mohammed Pourkashanian
Format: Journal
Published: 2018
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http://cmuir.cmu.ac.th/jspui/handle/6653943832/58647
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spelling th-cmuir.6653943832-586472018-09-05T04:27:34Z Simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: Optimization using the simplex lattice design Chawannat Jaroenkhasemmeesuk Maria Elena Diego Nakorn Tippayawong Derek B. Ingham Mohammed Pourkashanian Energy Copyright © 2018 John Wiley & Sons, Ltd. Bio-oil produced via fast pyrolysis of biomass usually has various undesired properties that can negatively affect its use. Therefore, raw bio-oil needs first to undergo an upgrading stage before it is further used. This paper deals with the study of bio-oil upgrading by means of catalytic cracking with a Y-zeolite/ZSM-5 catalyst, as well as the optimization of the process operating conditions. Several case studies are selected by using the simplex lattice design of experiments, and these are simulated under a range of conditions to study the effect of the key process parameters on the bio-oil conversion. The simulation results show that the catalyst-to-oil ratio is the most influential parameter. An analysis of the obtained data indicates that a Y-zeolite/ZSM-5 catalyst blend with 15.6 to 19.0%wt of Y-zeolite, a catalyst-to-oil ratio in the range of 4.9 to 6.1, a riser height of 24.6 to 30.0 m (residence time ~ 6 s), and a reactor temperature of 350 to 385°C are the preferred conditions that maximize the product conversion, which take values up to 78.5% in the simulations. A comparison against previous experimental results confirms that the value of the ratio between catalyst and bio-oil is a critical design parameter and highlights that the optimum values of the Y-zeolite content and the reactor temperature calculated from the simulation data are in good agreement with those obtained experimentally. The simulation analysis conducted in this study is a suitable tool to investigate the catalytic cracking process for bio-oil upgrading. 2018-09-05T04:27:34Z 2018-09-05T04:27:34Z 2018-07-01 Journal 1099114X 0363907X 2-s2.0-85042186696 10.1002/er.4023 https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=85042186696&origin=inward http://cmuir.cmu.ac.th/jspui/handle/6653943832/58647
institution Chiang Mai University
building Chiang Mai University Library
country Thailand
collection CMU Intellectual Repository
topic Energy
spellingShingle Energy
Chawannat Jaroenkhasemmeesuk
Maria Elena Diego
Nakorn Tippayawong
Derek B. Ingham
Mohammed Pourkashanian
Simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: Optimization using the simplex lattice design
description Copyright © 2018 John Wiley & Sons, Ltd. Bio-oil produced via fast pyrolysis of biomass usually has various undesired properties that can negatively affect its use. Therefore, raw bio-oil needs first to undergo an upgrading stage before it is further used. This paper deals with the study of bio-oil upgrading by means of catalytic cracking with a Y-zeolite/ZSM-5 catalyst, as well as the optimization of the process operating conditions. Several case studies are selected by using the simplex lattice design of experiments, and these are simulated under a range of conditions to study the effect of the key process parameters on the bio-oil conversion. The simulation results show that the catalyst-to-oil ratio is the most influential parameter. An analysis of the obtained data indicates that a Y-zeolite/ZSM-5 catalyst blend with 15.6 to 19.0%wt of Y-zeolite, a catalyst-to-oil ratio in the range of 4.9 to 6.1, a riser height of 24.6 to 30.0 m (residence time ~ 6 s), and a reactor temperature of 350 to 385°C are the preferred conditions that maximize the product conversion, which take values up to 78.5% in the simulations. A comparison against previous experimental results confirms that the value of the ratio between catalyst and bio-oil is a critical design parameter and highlights that the optimum values of the Y-zeolite content and the reactor temperature calculated from the simulation data are in good agreement with those obtained experimentally. The simulation analysis conducted in this study is a suitable tool to investigate the catalytic cracking process for bio-oil upgrading.
format Journal
author Chawannat Jaroenkhasemmeesuk
Maria Elena Diego
Nakorn Tippayawong
Derek B. Ingham
Mohammed Pourkashanian
author_facet Chawannat Jaroenkhasemmeesuk
Maria Elena Diego
Nakorn Tippayawong
Derek B. Ingham
Mohammed Pourkashanian
author_sort Chawannat Jaroenkhasemmeesuk
title Simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: Optimization using the simplex lattice design
title_short Simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: Optimization using the simplex lattice design
title_full Simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: Optimization using the simplex lattice design
title_fullStr Simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: Optimization using the simplex lattice design
title_full_unstemmed Simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: Optimization using the simplex lattice design
title_sort simulation analysis of the catalytic cracking process of biomass pyrolysis oil with mixed catalysts: optimization using the simplex lattice design
publishDate 2018
url https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=85042186696&origin=inward
http://cmuir.cmu.ac.th/jspui/handle/6653943832/58647
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