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Solid Acid Catalysts for
         Biomass Transformations



A.S. Rocha, D. R. Fernandes,   T.   Firmino,   E.   F.   Mai,   B.   L.   Oliveira,
and V. Teixeira da Silva




                     Thessaloniki, 31st October 2012
Residual Biomass Transformations
                   Residual Biomass



                 Hemicellulose, Cellulose


     Pentoses                           Hexoses
     (Xylose)                 (Glucose, Fructose, Mannose)
      H+   - H2O                            H+   - H2 O




      Furfural                5-Hydroxymethylfurfural (HMF)
                                                 H2O, H+




                                        Levulinic acid
Levulinic acid as a platform molecule




Corma, Iborra and Velty, Chem. Rev. 2007, 107, 2411-2502
Levulinic acid as a platform molecule




•   Food industry (flavors)
•   Solvents
•   Plasticizers
•   Diesel Miscible Biofuel
Levulinic acid as a platform molecule




•   Food industry (flavors)
•   Solvents
•   Plasticizers
•   Diesel Miscible Biofuel
                               www.dibanet.org
Ethyl levulinate synthesis
                                                                                       T = 343 K
                                                                                           t=5h
                                                                              2.5 wt.% of catalyst
                                                                                 EtOH/LvAc = 5/1
                                                                 2411
                                                                  747
                                                                 1867
                                                                 2181
                                                                 2414
                                                                2360
                                                                1167
                                                                 892
                                                                 584
                                                                 429
                                                                 342




D.R. Fernandes et al. Applied Catalysis A: General 425– 426 (2012) 199– 204
Sulfated stania
Catalyst synthesis




                                                                                     Solubilization
                                                                                     leading to a
                                                                                     low yield of
                                                                                     the dried gel



Arata, App. Catal. A 1996, 146, 3-32.
Matsuhashi, Miyazaki, Kawamura, Nakamura, Arata, Chem. Mater. 2001, 13, 3038-3042.
Catalyst synthesis




Arata, App. Catal. A 1996, 146, 3-32.
Matsuhashi, Miyazaki, Kawamura, Nakamura, Arata, Chem. Mater. 2001, 13, 3038-3042.
Catalyst characterization - XRD
Catalyst characterization - Raman
Catalyst characterization – N2
 physisorption

    Sample               Sg / m2 g-1
     SnO2                     40
SO4-2/ SnO2 (1M)             108
SO4-2/ SnO2 (2M)             120
SO4-2/ SnO2 (3M)             130
SO4-2/ SnO2 (4M)             140
SO4-2/ SnO2 (5M)             148
Characterization – SEM
Catalyst characterization - XRF



  Sample        %SO3     % SnO2       % Cl
    SnO2        0.004    99.902       0.094
SO4/SnO2 (1M)   4.503    95.478       0.019
SO4/SnO2 (2M)   5.046    94.921       0.033
SO4/SnO2 (3M)   5.309    94.659       0.032
SO4/SnO2 (4M)   5.280    94.660       0.059
SO4/SnO2 (5M)   5.025    94.926       0.046
Catalyst characterization – NH3 TPD

                                                                4.4 μmol m-2
                                                                6.0 μmol m-2

                                                                6.9 μmol m-2
m/z = 15 signal / A. U.




                                                                8.4 μmol m-2

                                                                7.2 μmol m-2

                                                                7.3 μmol m-2




                                  Temperature / oC
Modification of the sulfur incorporation
Characterization – N2 physisorption
Characterization – XRD
Characterization – XRD
Catalytic activity            T = 343 K
                                  t=5h
                     2.5 wt.% of catalyst
                        EtOH/LvAc = 5/1
Catalytic activity            T = 343 K
                                  t=5h
                     2.5 wt.% of catalyst
                        EtOH/LvAc = 5/1
Catalytic activity            T = 343 K
                                  t=5h
                     2.5 wt.% of catalyst
                        EtOH/LvAc = 5/1
Reusability – Amberlyst 15
Reusability – GIA-5%
Reusability – GIA-5%
Reusability – GIA-5%
Conclusions


•    For sulfated solid oxide catalyts there is a correlation between the
    total acidity and activity;
Conclusions


•    For sulfated solid oxide catalyts there is a correlation between the
    total acidity and activity;

•   For zeolites the pore structure seems to play a more important role
    than the total acidity;
Conclusions


•    For sulfated solid oxide catalyts there is a correlation between the
    total acidity and activity;

•   For zeolites the pore structure seems to play a more important role
    than the total acidity;

•   Sulfated stania presents a good activity in levulinic acid esterification
    but undergoes deactivation. Changing the washing procedure it is
    possible to reuse the catalyst.
Conclusions


•    For sulfated solid oxide catalyts there is a correlation between the
    total acidity and activity;

•   For zeolites the pore structure seems to play a more important role
    than the total acidity

•   Sulfated stania presents a good activity in levulinic acid esterification
    but undergoes deactivation. Changing the washing procedure it is
    possible to reuse the catalyst.

•   Amberlyst-15, a commercial available resin is active and stable in the
    liquid phase levulinic acid esterification with ethanol.
Acknowledgments




            This work was performed
            within the DIBANET Network,
            a project within the European
            Community’s Seventh
            Framework Programme
            (FP7/2007-2013) under grant
            agreement no: 227248-2.
Acknowledgments




Thanks for your
attention!
       ευχαριστώ!
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Solid acid catalysts for biomass transformations

  • 1. Solid Acid Catalysts for Biomass Transformations A.S. Rocha, D. R. Fernandes, T. Firmino, E. F. Mai, B. L. Oliveira, and V. Teixeira da Silva Thessaloniki, 31st October 2012
  • 2. Residual Biomass Transformations Residual Biomass Hemicellulose, Cellulose Pentoses Hexoses (Xylose) (Glucose, Fructose, Mannose) H+ - H2O H+ - H2 O Furfural 5-Hydroxymethylfurfural (HMF) H2O, H+ Levulinic acid
  • 3. Levulinic acid as a platform molecule Corma, Iborra and Velty, Chem. Rev. 2007, 107, 2411-2502
  • 4. Levulinic acid as a platform molecule • Food industry (flavors) • Solvents • Plasticizers • Diesel Miscible Biofuel
  • 5. Levulinic acid as a platform molecule • Food industry (flavors) • Solvents • Plasticizers • Diesel Miscible Biofuel www.dibanet.org
  • 6. Ethyl levulinate synthesis T = 343 K t=5h 2.5 wt.% of catalyst EtOH/LvAc = 5/1 2411 747 1867 2181 2414 2360 1167 892 584 429 342 D.R. Fernandes et al. Applied Catalysis A: General 425– 426 (2012) 199– 204
  • 8. Catalyst synthesis Solubilization leading to a low yield of the dried gel Arata, App. Catal. A 1996, 146, 3-32. Matsuhashi, Miyazaki, Kawamura, Nakamura, Arata, Chem. Mater. 2001, 13, 3038-3042.
  • 9. Catalyst synthesis Arata, App. Catal. A 1996, 146, 3-32. Matsuhashi, Miyazaki, Kawamura, Nakamura, Arata, Chem. Mater. 2001, 13, 3038-3042.
  • 12. Catalyst characterization – N2 physisorption Sample Sg / m2 g-1 SnO2 40 SO4-2/ SnO2 (1M) 108 SO4-2/ SnO2 (2M) 120 SO4-2/ SnO2 (3M) 130 SO4-2/ SnO2 (4M) 140 SO4-2/ SnO2 (5M) 148
  • 14. Catalyst characterization - XRF Sample %SO3 % SnO2 % Cl SnO2 0.004 99.902 0.094 SO4/SnO2 (1M) 4.503 95.478 0.019 SO4/SnO2 (2M) 5.046 94.921 0.033 SO4/SnO2 (3M) 5.309 94.659 0.032 SO4/SnO2 (4M) 5.280 94.660 0.059 SO4/SnO2 (5M) 5.025 94.926 0.046
  • 15. Catalyst characterization – NH3 TPD 4.4 μmol m-2 6.0 μmol m-2 6.9 μmol m-2 m/z = 15 signal / A. U. 8.4 μmol m-2 7.2 μmol m-2 7.3 μmol m-2 Temperature / oC
  • 16. Modification of the sulfur incorporation
  • 17. Characterization – N2 physisorption
  • 20. Catalytic activity T = 343 K t=5h 2.5 wt.% of catalyst EtOH/LvAc = 5/1
  • 21. Catalytic activity T = 343 K t=5h 2.5 wt.% of catalyst EtOH/LvAc = 5/1
  • 22. Catalytic activity T = 343 K t=5h 2.5 wt.% of catalyst EtOH/LvAc = 5/1
  • 27. Conclusions • For sulfated solid oxide catalyts there is a correlation between the total acidity and activity;
  • 28. Conclusions • For sulfated solid oxide catalyts there is a correlation between the total acidity and activity; • For zeolites the pore structure seems to play a more important role than the total acidity;
  • 29. Conclusions • For sulfated solid oxide catalyts there is a correlation between the total acidity and activity; • For zeolites the pore structure seems to play a more important role than the total acidity; • Sulfated stania presents a good activity in levulinic acid esterification but undergoes deactivation. Changing the washing procedure it is possible to reuse the catalyst.
  • 30. Conclusions • For sulfated solid oxide catalyts there is a correlation between the total acidity and activity; • For zeolites the pore structure seems to play a more important role than the total acidity • Sulfated stania presents a good activity in levulinic acid esterification but undergoes deactivation. Changing the washing procedure it is possible to reuse the catalyst. • Amberlyst-15, a commercial available resin is active and stable in the liquid phase levulinic acid esterification with ethanol.
  • 31. Acknowledgments This work was performed within the DIBANET Network, a project within the European Community’s Seventh Framework Programme (FP7/2007-2013) under grant agreement no: 227248-2.