Highly selective oxidation of glucose to formic acid and exploring reaction pathways using continuous flow microreactors
Highly selective oxidation of glucose to formic acid and exploring reaction pathways using continuous flow microreactors
The process of converting glucose into formic acid (FA) has been explored as a promising route for using biomass as a renewable feedstock for green chemical manufacturing. However, the most commonly used batch-tank reactor systems currently suffer from several drawbacks, including extended processing time, limited product selectivity, and high energy consumption, while the underlying reaction paths have been poorly understood. In this work, a continuous flow microchannel reactor was employed for the glucose conversion catalyzed by H5PV2Mo10O40 with O2 as an oxidant. The influence of various parameters on the conversion rate of glucose and the FA yield was characterized. Experimental results indicated that with a residence time of less than 3 min, the glucose was completely converted, and the highest FA yield reached 82.40 %. Extensive examination on the apparent by-products revealed that most of them acted as intermediates to produce FA through various pathways, including glyoxal, glyceraldehyde and glycolaldehyde as key intermediates for the oxidation of glucose to FA. Furthermore, the density functional theory (DFT) method was used to determine the bond energies of different C–C bond cleavage modes of substrate glucose and fructose produced by the isomerization of glucose. Experimentally, the conversion of three main intermediates and some other possible intermediates and their FA yield were measured with different residence time. It was also found that the CO2 was produced through the decarboxylation of α-hydroxy and α-carbonyl carboxylic acid compounds, while the aldehyde groups in the compounds were more likely converted to FA by the α-carbon bond cleavage. Finally, plausible reaction pathways were proposed for the process of glucose-to-FA catalyzed by HPA-2, providing useful guidance for the identification of side reaction pathways and further improvement of FA yield.
Formic acid, Glucose, Microchannel, Microreactor, Process intensification
Wei, Xing
cb6cad92-88d0-43d9-8142-fb08ae25a34f
Wang, Qingqiang
5f80e94c-3f20-4923-9f5b-aa532056083f
Zhang, Xunli
d7cf1181-3276-4da1-9150-e212b333abb1
Chen, Ying
074945eb-ea1b-47f2-92be-c286a8134388
Jin, Nan
4c238610-7344-4b96-aeef-f039b663691c
Zhao, Yuchao
0b5eafdf-0011-4a02-840f-e5b88b61a708
15 September 2024
Wei, Xing
cb6cad92-88d0-43d9-8142-fb08ae25a34f
Wang, Qingqiang
5f80e94c-3f20-4923-9f5b-aa532056083f
Zhang, Xunli
d7cf1181-3276-4da1-9150-e212b333abb1
Chen, Ying
074945eb-ea1b-47f2-92be-c286a8134388
Jin, Nan
4c238610-7344-4b96-aeef-f039b663691c
Zhao, Yuchao
0b5eafdf-0011-4a02-840f-e5b88b61a708
Wei, Xing, Wang, Qingqiang, Zhang, Xunli, Chen, Ying, Jin, Nan and Zhao, Yuchao
(2024)
Highly selective oxidation of glucose to formic acid and exploring reaction pathways using continuous flow microreactors.
Fuel, 372, [132198].
(doi:10.1016/j.fuel.2024.132198).
Abstract
The process of converting glucose into formic acid (FA) has been explored as a promising route for using biomass as a renewable feedstock for green chemical manufacturing. However, the most commonly used batch-tank reactor systems currently suffer from several drawbacks, including extended processing time, limited product selectivity, and high energy consumption, while the underlying reaction paths have been poorly understood. In this work, a continuous flow microchannel reactor was employed for the glucose conversion catalyzed by H5PV2Mo10O40 with O2 as an oxidant. The influence of various parameters on the conversion rate of glucose and the FA yield was characterized. Experimental results indicated that with a residence time of less than 3 min, the glucose was completely converted, and the highest FA yield reached 82.40 %. Extensive examination on the apparent by-products revealed that most of them acted as intermediates to produce FA through various pathways, including glyoxal, glyceraldehyde and glycolaldehyde as key intermediates for the oxidation of glucose to FA. Furthermore, the density functional theory (DFT) method was used to determine the bond energies of different C–C bond cleavage modes of substrate glucose and fructose produced by the isomerization of glucose. Experimentally, the conversion of three main intermediates and some other possible intermediates and their FA yield were measured with different residence time. It was also found that the CO2 was produced through the decarboxylation of α-hydroxy and α-carbonyl carboxylic acid compounds, while the aldehyde groups in the compounds were more likely converted to FA by the α-carbon bond cleavage. Finally, plausible reaction pathways were proposed for the process of glucose-to-FA catalyzed by HPA-2, providing useful guidance for the identification of side reaction pathways and further improvement of FA yield.
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JFUE-D-24-00730_Accepted
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Accepted/In Press date: 18 June 2024
e-pub ahead of print date: 18 June 2024
Published date: 15 September 2024
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© 2024 Elsevier Ltd
Keywords:
Formic acid, Glucose, Microchannel, Microreactor, Process intensification
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Local EPrints ID: 491575
URI: http://eprints.soton.ac.uk/id/eprint/491575
ISSN: 0016-2361
PURE UUID: 323bd9f4-8838-4c4b-988f-b0447214d29e
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Date deposited: 27 Jun 2024 16:35
Last modified: 12 Jul 2024 01:45
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Contributors
Author:
Xing Wei
Author:
Qingqiang Wang
Author:
Ying Chen
Author:
Nan Jin
Author:
Yuchao Zhao
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