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- korean
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- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received July 27, 2023
Revised August 17, 2023
Accepted September 25, 2023
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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포름산 및 황산 촉매를 이용한 자일로스로부터 푸르푸랄 생산
Furfural Production From Xylose by Using Formic Acid and Sulfuric Acid
Abstract
푸르푸랄(furfural)은 리그노셀룰로오스 바이오매스(lignocellulose biomass)의 헤미셀룰로오스(hemicellulose) 성
분 중 하나인 자일로스(xylose)로부터 생산되는 플랫폼 화학물질이다. 푸르푸랄은 페놀류 화합물이나 바이오 연
료 등의 중요한 원료로 사용될 수 있다. 본 연구에서는 푸르푸랄 생산공정에서 일반적으로 사용되는 산 촉매인
황산(sulfuric acid)과 친환경적 촉매인 포름산(formic acid) 두 가지 촉매를 이용하여 회분식 반응 시스템(batch
system)에서 자일로스로부터 푸르푸랄을 생산하기 위한 조건을 비교 및 최적화하였다. 자일로스의 초기 농도(10 g/
L~100 g/L), 반응 온도(140~200℃), 황산 촉매(1~3 wt%), 포름산 촉매(5~10 wt%), 반응 시간에 따라 자일로스로
부터 푸르푸랄 수율에 미치는 영향을 조사하였다. 촉매 종류에 따른 최적 조건은 다음과 같았다. 황산 촉매의 경
우, 3 wt%의 촉매농도, 50 g/L의 초기 자일로스 농도, 180 ℃의 온도 10분의 반응시간에서 최대 58.97%의 푸르
푸랄 수율을 얻었다. 포름산 촉매의 겨우, 5 wt%의 촉매농도, 50 g/L의 초기 자일로스 농도, 180 ℃의 온도, 150
분 반응 시간에서 65.32%의 푸르푸랄 수율을 확보하였다.
Furfural is a platform chemical that is produced from xylose, one of the hemicellulose components of
lignocellulosic biomass. Furfural can be used as an important feedstock for phenolic compounds or biofuels. In this
study, we compared and optimized the conditions for producing furfural from xylose in a batch system using two types
of catalysts: sulfuric acid, which is commonly used in the furfural production process, and formic acid, which is an
environmentally friendly catalyst. We investigated the effects of xylose initial concentration (10 g/L~100 g/L), reaction
temperature (140~200℃), sulfuric acid catalyst (1~3 wt%), formic acid catalyst (5~10 wt%), and reaction time on the
furfural yield. The optimal conditions according to the type of catalyst were as follows. For sulfuric acid catalyst, 3 wt%
of catalyst concentration, 50 g/L of xylose initial concentration, 180℃ of temperature, and 10min of reaction time
resulted in a maximum furfural yield of 59.0%. For formic acid catalyst, 5 wt% of catalyst concentration, 50 g/L of
xylose initial concentration, 180℃ of temperature, and 150 min of reaction time resulted in a furfural yield of 65.3%.
References
L. and Zhao, Z. P., “Fast and Continuous Conversion of Xylose
to Furfural in Micropacked Bed Reactors,” Chemical Engineering
Science, 266, 118256(2023).
2. Yan, K., Wu, G., Lafleur, T. and Jarvis, C., “Production, Properties
and Catalytic Hydrogenation of Furfural to Fuel Additives
and Value-added Chemicals,” Renewable and Sustainable Energy
Reviews, 38, 663-676(2014).
3. Yemiş, O. and Mazza, G., “Acid-catalyzed Conversion of Xylose,
Xylan and Straw Into Furfural by Microwave-assisted Reaction,”
Bioresource Technology, 102(15), 7371-7378(2011).
4. Machado, G., Leon, S., Santos, F., Lourega, R., Dullius, J., Mollmann,
M. E. and Eichler, P., “Literature Review on Furfural Production
From Lignocellulosic Biomass,” Natural Resources, 7(3),115-129(2011).
5. Adhami, W., Richel, A. and Len, C., “A Review of Recent Advances
in the Production of Furfural in Batch System,” Molecular Catalysis,
545, 113178(2023).
6. Modelska, M., Binczarski, M. J., Dziugan, P., Nowak, S., Romanowska-
Duda, Z., Sadowski, A. and Witońska, I. A., “Potential
of Waste Biomass From the Sugar Industry as a Source of Furfural
and Its Derivatives for Use as Fuel Additives in Poland,” Energies,
13(24), 6684(2020).
7. Liu, Y., Ma, C., Huang, C., Fu, Y. and Chang, J., “Efficient Conversion
of Xylose Into Furfural Using Sulfonic Acid-functionalized
Metal–organic Frameworks in a Biphasic System,” Industrial &
Engineering Chemistry Research, 57(49), 16628-16634(2018).
8. Jin, S., Hao, Z., Zhang, K., Yan, Z. and Chen, J., “Advances and
Challenges for the Electrochemical Reduction of CO2 to CO:
From Fundamentals to Industrialization,” Angewandte Chemie,
133(38), 20795-20816(2021).
9. Vogt, C. and Weckhuysen, B. M., “The Concept of Active Site
in Heterogeneous Catalysis,” Nature Reviews Chemistry, 6(2),
89-111(2022).
10. Hu, S. L., Cheng, H., Xu, R. Y., Huang, J. S., Zhang, P. J. and
Qin, J. N., “Conversion of Xylose Into Furfural Over Cr/Mg
Hydrotalcite Catalysts,” Molecular Catalysis, 538, 113009(2023).
11. Yang, W., Li, P., Bo, D. and Chang, H., “The Optimization of
Formic Acid Hydrolysis of Xylose in Furfural Production,” Carbohydrate
Research, 357, 53-61(2012).
12. Suxia, R., Haiyan, X., Jinling, Z., Shunqing, L., Xiaofeng, H.
and Tingzhou, L., “Furfural Production From Rice Husk Using
Sulfuric Acid and a Solid Acid Catalyst Through a Two-stage
Rocess,” Carbohydrate Research, 359, 1-6(2012).
13. Tongtummachat, T., Jaree, A. and Akkarawatkhoosith, N., “Continuous
Hydrothermal Furfural Production From Xylose in a Microreactor
with Dual-acid Catalysts,” RSC Advances, 12(36), 23366-
23378(2022).
14. Zhang, X., Xu, S., Li, Q., Zhou, G. and Xia, H., “Recent Advances in
the Conversion of Furfural Into Bio-chemicals Through Chemoand
Bio-catalysis,” RSC Advances, 11(43), 27042-27058(2021).
15. Xu, S., Yang, J., Li, J. and Shen, F., “Highly Efficient Oxidation
of Biomass Xylose to Formic Acid with CeO x-Promoted MnOx
Catalyst in Water,” ACS Sustainable Chemistry & Engineering
(2023).
16. Almhofer, L., Bischof, R. H., Madera, M. and Paulik, C., “Kinetic
and Mechanistic Aspects of Furfural Degradation in Biorefineries,”
The Canadian Journal of Chemical Engineering, 101(4),
2033-2049(2023).
17. Yang, W., Li, P., Bo, D., Chang, H., Wang, X. and Zhu, T.,
“Optimization of Furfural Production From D-xylose with Formic
Acid as Catalyst in a Reactive Extraction System,” Bioresource
Technology, 133, 361-369(2013).
18. de Carvalho, R. S., de A. Rodrigues, F., Monteiro, R. S. and da
Silva Faria, W. L., “Optimization of Furfural Synthesis From Xylose
Using Niobic Acid and Niobium Phosphate as Catalysts,” Waste
and Biomass Valorization, 10, 2673-2680(2019).
19. Köchermann, J., Schreiber, J. and Klemm, M., “Conversion of
D-xylose and Hemicellulose in Water/ethanol Mixtures,” ACS
Sustainable Chemistry & Engineering, 7(14), 12323-12330(2019).
20. Choudhary, V., Sandler, S. I. and Vlachos, D. G., “Conversion of
Xylose to Furfural Using Lewis and Brønsted Acid Catalysts in
Aqueous Media,” Acs Catalysis, 2(9), 2022-2028(2012).
21. Lee, S. M., Han, S. and Kim, J. S., “Levulinic Acid Production
from Lignocellulosic Biomass by co-solvent Pretreatment with
NaOH/THF,” Korean Chemical Engineering Research, 61(2),
265-272(2023).
22. Yang, T., Li, W., Su, M., Liu, Y. and Liu, M., “Production of
Furfural From Xylose Catalyzed by a Novel Calcium Gluconate
Derived Carbon Solid Acid in 1,4-dioxane,” New Journal of
Chemistry, 44(19), 7968-7975(2020).
23. Han, S., Lee, S. M. and Kim, J. S., “Kinetic Study of Glucose
Conversion to 5-hydroxymethylfurfural and Levulinic Acid Catalyzed
by Sulfuric Acid,” Korean Chemical Engineering Research,
60(2), 193-201(2022).