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Title: Catalytic hydrogenation of dihydrolevoglucosenone to levoglucosanol with a hydrotalcite/mixed oxide copper catalyst

Abstract

Levoglucosanol (LGOL) is a critical intermediate for the bio-based production of hexane-1,2,5,6-tetrol, 1,2,6-hexanetriol, and 1,6-hexanediol. Here we report on the aqueous-phase hydrogenation of cellulose-derived dihydrolevoglucosenone (Cyrene™) to LGOL using a calcined and reduced heterogeneous copper/hydrotalcite/mixed oxide catalyst, denoted as Cu8/MgAlOx-HP. The turnover frequency for LGOL conversion over this copper-containing catalyst is equal to 0.013 s–1 at 353 K as measured in a flow reactor which is half the one obtained using 0.4 wt% Pd/Al2O3. Moreover, while Cu8/MgAlOx-HP shows a stable activity, the activity of 0.4 wt% Pd/Al2O3 decreases with time-on-stream. Neither Cu- nor Al-leaching is observed (resp. <1 ppb and <1 ppm) but Mg leaching can be seen (5.5 ppm). The latter leaching relates to the acidity of the Cyrene/H2O mixture (pH 3.5–4.5 range), which is due to the occurrence of the geminal diol moiety of Cyrene, an acidic species. In contrast, additional and consecutive oxidation and reduction of the catalyst leads to a gradual decrease in activity over time. Applying still further oxidation/reduction cycles to this catalyst tends to decrease its activity with some overall stabilization being observed from the fourth run onwards. Mg-leaching is shown to change the relative meso-to-macro pore content, but leaves the total pore volumemore » unchanged between the fresh and the spent catalyst. In spite of the high copper loading (8 wt%), small Cu-nanoparticles (2–3 nm) are present over the hydrotalcite/mixed oxide surface of the Cu8/MgAlOx-HP material, and these particles do not aggregate during the hydrogenation reaction.« less

Authors:
ORCiD logo [1]; ORCiD logo [2]; ORCiD logo [3]; ORCiD logo [4]; ORCiD logo [2]; ORCiD logo [2];  [2]; ORCiD logo [3]; ORCiD logo [2]; ORCiD logo [2]; ORCiD logo [5]
  1. Department of chemical and biological engineering, University of Wisconsin-Madison, 53706 Wisconsin, USA, Faculty of Science
  2. Department of chemical and biological engineering, University of Wisconsin-Madison, 53706 Wisconsin, USA
  3. Instituto de Química, Unesp - Universidade Estadual Paulista, Araraquara, Brazil
  4. Department of chemical and biological engineering, University of Wisconsin-Madison, 53706 Wisconsin, USA, DOE Center for Advanced Bioenergy and Bioproducts Innovation
  5. Faculty of Science, Debye Institute for Nanomaterials Science, Utrecht University, CGUtrecht 3584, The Netherlands
Publication Date:
Research Org.:
Center for Advanced Bioenergy and Bioproducts Innovation, Urbana, IL (United States)
Sponsoring Org.:
USDOE Office of Science (SC), Biological and Environmental Research (BER)
OSTI Identifier:
1557907
Alternate Identifier(s):
OSTI ID: 1561043
Grant/Contract Number:  
SC0018420
Resource Type:
Published Article
Journal Name:
Green Chemistry
Additional Journal Information:
Journal Name: Green Chemistry Journal Volume: 21 Journal Issue: 18; Journal ID: ISSN 1463-9262
Publisher:
Royal Society of Chemistry (RSC)
Country of Publication:
United Kingdom
Language:
English
Subject:
37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY

Citation Formats

De bruyn, Mario, Sener, Canan, Petrolini, Davi D., McClelland, Daniel J., He, Jiayue, Ball, Madelyn R., Liu, Yifei, Martins, Leandro, Dumesic, James A., Huber, George W., and Weckhuysen, Bert M. Catalytic hydrogenation of dihydrolevoglucosenone to levoglucosanol with a hydrotalcite/mixed oxide copper catalyst. United Kingdom: N. p., 2019. Web. doi:10.1039/C9GC00564A.
De bruyn, Mario, Sener, Canan, Petrolini, Davi D., McClelland, Daniel J., He, Jiayue, Ball, Madelyn R., Liu, Yifei, Martins, Leandro, Dumesic, James A., Huber, George W., & Weckhuysen, Bert M. Catalytic hydrogenation of dihydrolevoglucosenone to levoglucosanol with a hydrotalcite/mixed oxide copper catalyst. United Kingdom. https://doi.org/10.1039/C9GC00564A
De bruyn, Mario, Sener, Canan, Petrolini, Davi D., McClelland, Daniel J., He, Jiayue, Ball, Madelyn R., Liu, Yifei, Martins, Leandro, Dumesic, James A., Huber, George W., and Weckhuysen, Bert M. Mon . "Catalytic hydrogenation of dihydrolevoglucosenone to levoglucosanol with a hydrotalcite/mixed oxide copper catalyst". United Kingdom. https://doi.org/10.1039/C9GC00564A.
@article{osti_1557907,
title = {Catalytic hydrogenation of dihydrolevoglucosenone to levoglucosanol with a hydrotalcite/mixed oxide copper catalyst},
author = {De bruyn, Mario and Sener, Canan and Petrolini, Davi D. and McClelland, Daniel J. and He, Jiayue and Ball, Madelyn R. and Liu, Yifei and Martins, Leandro and Dumesic, James A. and Huber, George W. and Weckhuysen, Bert M.},
abstractNote = {Levoglucosanol (LGOL) is a critical intermediate for the bio-based production of hexane-1,2,5,6-tetrol, 1,2,6-hexanetriol, and 1,6-hexanediol. Here we report on the aqueous-phase hydrogenation of cellulose-derived dihydrolevoglucosenone (Cyrene™) to LGOL using a calcined and reduced heterogeneous copper/hydrotalcite/mixed oxide catalyst, denoted as Cu8/MgAlOx-HP. The turnover frequency for LGOL conversion over this copper-containing catalyst is equal to 0.013 s–1 at 353 K as measured in a flow reactor which is half the one obtained using 0.4 wt% Pd/Al2O3. Moreover, while Cu8/MgAlOx-HP shows a stable activity, the activity of 0.4 wt% Pd/Al2O3 decreases with time-on-stream. Neither Cu- nor Al-leaching is observed (resp. <1 ppb and <1 ppm) but Mg leaching can be seen (5.5 ppm). The latter leaching relates to the acidity of the Cyrene/H2O mixture (pH 3.5–4.5 range), which is due to the occurrence of the geminal diol moiety of Cyrene, an acidic species. In contrast, additional and consecutive oxidation and reduction of the catalyst leads to a gradual decrease in activity over time. Applying still further oxidation/reduction cycles to this catalyst tends to decrease its activity with some overall stabilization being observed from the fourth run onwards. Mg-leaching is shown to change the relative meso-to-macro pore content, but leaves the total pore volume unchanged between the fresh and the spent catalyst. In spite of the high copper loading (8 wt%), small Cu-nanoparticles (2–3 nm) are present over the hydrotalcite/mixed oxide surface of the Cu8/MgAlOx-HP material, and these particles do not aggregate during the hydrogenation reaction.},
doi = {10.1039/C9GC00564A},
journal = {Green Chemistry},
number = 18,
volume = 21,
place = {United Kingdom},
year = {Mon Sep 16 00:00:00 EDT 2019},
month = {Mon Sep 16 00:00:00 EDT 2019}
}

Journal Article:
Free Publicly Available Full Text
Publisher's Version of Record
https://doi.org/10.1039/C9GC00564A

Citation Metrics:
Cited by: 14 works
Citation information provided by
Web of Science

Figures / Tables:

Fig. 1 Fig. 1: Overview of the synthetic possibilities starting from levoglucosanol (LGOL) as a platform molecule.

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