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Reaction microkinetic model of xylose dehydration to furfural over beta zeolite catalyst
ID
Rakić, Emilija
(
Author
),
ID
Kostyniuk, Andrii
(
Author
),
ID
Nikačević, Nikola
(
Author
),
ID
Likozar, Blaž
(
Author
)
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MD5: 9AD01A119EB623AC327E1E726E4565C2
URL - Source URL, Visit
https://link.springer.com/article/10.1007/s13399-023-04969-1
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Abstract
In recent decades, there has been a growing interest in bio-refineries as a crucial element in transitioning to a low-carbon economy. One specific aspect of this interest is the conversion of carbohydrates into separate platform chemicals, such as furfural (FUR), which play a significant functional role in various daily life processes. This research paper focuses on investigating the use of a H-beta catalyst with SiO$_2$/Al$_2$O$_3$ = 28 for producing furfural from xylose in water. Various conditions, such as temperature and initial solution concentration, are studied to determine their effect on FUR yield. The highest FUR yield (40 mol.%) is obtained when FUR is the only product species. We also report that about 90% yield from reaction with fresh catalyst can be achieved after catalyst regeneration. The activation energies for the reaction on the catalyst surface are found to be in the range of 38–75 kJ/mol. A mathematical kinetic model with three irreversible steps is derived to estimate the reaction sequence at 160, 180, and 200 °C. The model takes into account mechanisms such as adsorption, desorption, and transport (internal or external). Our results suggest that the H-beta catalyst shows high activity toward FUR yield and could be a promising alternative for mass-scale production of the latter.
Language:
English
Keywords:
xylose
,
furfural
,
dehydration
,
reaction
,
microkinetic model
Work type:
Article
Typology:
1.01 - Original Scientific Article
Organization:
FKKT - Faculty of Chemistry and Chemical Technology
Publication status:
Published
Publication version:
Version of Record
Year:
2025
Number of pages:
Str. 2303–2317
Numbering:
Vol. 15, iss. 2
PID:
20.500.12556/RUL-166700
UDC:
66
ISSN on article:
2190-6823
DOI:
10.1007/s13399-023-04969-1
COBISS.SI-ID:
171108611
Publication date in RUL:
22.01.2025
Views:
547
Downloads:
1327
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Record is a part of a journal
Title:
Biomass conversion and biorefinery
Shortened title:
Biomass convers. biorefin.
Publisher:
Springer Nature
ISSN:
2190-6823
COBISS.SI-ID:
520489241
Licences
License:
CC BY 4.0, Creative Commons Attribution 4.0 International
Link:
http://creativecommons.org/licenses/by/4.0/
Description:
This is the standard Creative Commons license that gives others maximum freedom to do what they want with the work as long as they credit the author.
Secondary language
Language:
Slovenian
Keywords:
kemijska tehnologija
,
katalizatorji
,
kinetični modeli
,
matematični modeli
Projects
Funder:
EC - European Commission
Funding programme:
H2020
Project number:
887226
Name:
Improve biorefinery operations through process intensification and new end products
Acronym:
BioSPRINT
Funder:
ARRS - Slovenian Research Agency
Project number:
P2-0152
Name:
Kemijsko reakcijsko inženirstvo
Funder:
ARRS - Slovenian Research Agency
Project number:
J2-2492
Name:
Razvoj procesov valorizacije lignina kot vira aromatskih gradnikov za proizvodnjo bioosnovanih polimerov
Funder:
ARRS - Slovenian Research Agency
Project number:
J2-1723
Name:
Katalitska pretvorba lignina v bioosnovane polimerne gradnike z uporabo CO2 (CaLiBration)
Funder:
ARRS - Slovenian Research Agency
Project number:
J7-1816
Name:
Krožna sinteza trajnostnih (bio)kemijskih procesov na osnovi obnovljivih virov
Funder:
ARRS - Slovenian Research Agency
Project number:
BI-RS/20-21-002
Funder:
Other - Other funder or multiple funders
Funding programme:
Science Fund of the Republic of Serbia
Funder:
ARRS - Slovenian Research Agency
Project number:
J1-3020
Name:
Uporaba odpadne biomase za katalitično pretvorbo v glukarno kislino: od večnivojskega reakcijskega modeliranja do reaktorske proizvodnje
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