TY - JOUR
T1 - H3PW12O40/SiO2 for sorbitol dehydration to isosorbide
T2 - High efficient and reusable solid acid catalyst
AU - Sun, Peng
AU - Yu, Ding Hua
AU - Hu, Yi
AU - Tang, Zhen Chen
AU - Xia, Jiao Jiao
AU - Li, Heng
AU - Huang, He
PY - 2011/1
Y1 - 2011/1
N2 - Tungstophosphoric acids (PW) supported on various metal oxides (SiO2, γ-Al2O3, TiO2, ZrO2 and CeO2) were synthesized and used as catalysts for sorbitol dehydration to isosorbide for the first time. 30% PW/SiO2 exhibited the best catalytic performance for sorbitol dehydration, over which 56% isosorbide selectivity could be gained at a 95% sorbitol conversion at 250 °C. The catalytic performance of regenerated 30% PW/SiO2 catalysts by dichloromethane elution showed no loss after recycling five runs. Characterizations with UV-Vis, XRD, NH3-TPD and thermal analysis techniques revealed that PW had a good dispersion, and the primary Keggin structure was preserved after supporting PW on different supports. The interaction between PW and oxides resulted in different acidity of catalysts, which affected conversion of sorbitol and selectivity for isosorbide. The final acidity order of supported PW catalysts was the following: SiO2<γ-Al2O32 ≈ ZrO22.
AB - Tungstophosphoric acids (PW) supported on various metal oxides (SiO2, γ-Al2O3, TiO2, ZrO2 and CeO2) were synthesized and used as catalysts for sorbitol dehydration to isosorbide for the first time. 30% PW/SiO2 exhibited the best catalytic performance for sorbitol dehydration, over which 56% isosorbide selectivity could be gained at a 95% sorbitol conversion at 250 °C. The catalytic performance of regenerated 30% PW/SiO2 catalysts by dichloromethane elution showed no loss after recycling five runs. Characterizations with UV-Vis, XRD, NH3-TPD and thermal analysis techniques revealed that PW had a good dispersion, and the primary Keggin structure was preserved after supporting PW on different supports. The interaction between PW and oxides resulted in different acidity of catalysts, which affected conversion of sorbitol and selectivity for isosorbide. The final acidity order of supported PW catalysts was the following: SiO2<γ-Al2O32 ≈ ZrO22.
KW - Dehydration
KW - Isosorbide
KW - Regeneration
KW - Sorbitol
KW - Tungstophosphoric Acid
UR - http://www.scopus.com/inward/record.url?scp=78650735478&partnerID=8YFLogxK
U2 - 10.1007/s11814-010-0324-2
DO - 10.1007/s11814-010-0324-2
M3 - 文章
AN - SCOPUS:78650735478
SN - 0256-1115
VL - 28
SP - 99
EP - 105
JO - Korean Journal of Chemical Engineering
JF - Korean Journal of Chemical Engineering
IS - 1
ER -