TY - JOUR
T1 - Maleic anhydride hydrogenation to succinic anhydride over mesoporous Ni/TiO2 catalysts
T2 - Effects of Ni loading and temperature
AU - Torres, Cecilia C.
AU - Alderete, Joel B.
AU - Mella, Claudio
AU - Pawelec, Barbara
N1 - Funding Information:
The authors thank FONDECYT postdoctoral grant 3140157 . C. Mella thanks CONICYT for doctoral fellowship 21150195 . B. Pawelec expresses her gratitude to Comunidad de Madrid (Project CAM S2013/MAE-2882 ) for their financial support.
Publisher Copyright:
© 2016 Elsevier B.V.
PY - 2016/11/1
Y1 - 2016/11/1
N2 - Catalytic hydrogenation of maleic anhydride for the production of succinic anhydride can be a viable alternative to the higher energetic demand route based in the dehydration of succinic acid. In this sense, the metallic Ni catalysts supported on mesoporous TiO2 (anatase) substrate demonstrated to be very active and 100% selective in the liquid phase hydrogenation of maleic anhydride (MA) to succinic anhydride (SA). The catalysts, which were prepared via wet impregnation method with different Ni loading (5, 10 and 15 wt.%), were characterized by chemical analysis (ICP-AES), N2 physical adsorption-desorption, H2-temperature programmed reduction (H2-TPR), X-ray diffraction (XRD), high resolution transmission electron spectroscopy (HR-TEM) and X-ray photoelectron spectroscopy (XPS). The Ni species interaction with support was investigated by TPR and by performing five catalyst recycling tests. After catalyst activation by reduction, the increase of Ni particle size with an increase of Ni loading was relatively small (from 6.9 to 8.9 nm) due to enhance of the metal-support interaction. After the first catalytic cycle, the optimized 5%Ni/TiO2 catalyst showed a small decrease in the Ni loading attributed to metal leaching during time course of reaction. Besides this, the 5%Ni/TiO2 catalyst exhibited a good stability during five continuous cycles with a very high yield of SA after 5 cycles. Finally, temperature experiments performed for the best system shown that the reaction temperature does not affect the SA selectivity in the temperature range studied (323 K–398 K).
AB - Catalytic hydrogenation of maleic anhydride for the production of succinic anhydride can be a viable alternative to the higher energetic demand route based in the dehydration of succinic acid. In this sense, the metallic Ni catalysts supported on mesoporous TiO2 (anatase) substrate demonstrated to be very active and 100% selective in the liquid phase hydrogenation of maleic anhydride (MA) to succinic anhydride (SA). The catalysts, which were prepared via wet impregnation method with different Ni loading (5, 10 and 15 wt.%), were characterized by chemical analysis (ICP-AES), N2 physical adsorption-desorption, H2-temperature programmed reduction (H2-TPR), X-ray diffraction (XRD), high resolution transmission electron spectroscopy (HR-TEM) and X-ray photoelectron spectroscopy (XPS). The Ni species interaction with support was investigated by TPR and by performing five catalyst recycling tests. After catalyst activation by reduction, the increase of Ni particle size with an increase of Ni loading was relatively small (from 6.9 to 8.9 nm) due to enhance of the metal-support interaction. After the first catalytic cycle, the optimized 5%Ni/TiO2 catalyst showed a small decrease in the Ni loading attributed to metal leaching during time course of reaction. Besides this, the 5%Ni/TiO2 catalyst exhibited a good stability during five continuous cycles with a very high yield of SA after 5 cycles. Finally, temperature experiments performed for the best system shown that the reaction temperature does not affect the SA selectivity in the temperature range studied (323 K–398 K).
KW - Hydrogenation
KW - Maleic anhydride
KW - Nickel
KW - Recycle
KW - Succinic anhydride
UR - http://www.scopus.com/inward/record.url?scp=84979892881&partnerID=8YFLogxK
U2 - 10.1016/j.molcata.2016.07.037
DO - 10.1016/j.molcata.2016.07.037
M3 - Article
AN - SCOPUS:84979892881
SN - 1381-1169
VL - 423
SP - 441
EP - 448
JO - Journal of Molecular Catalysis A: Chemical
JF - Journal of Molecular Catalysis A: Chemical
ER -