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Catalytic Fast Pyrolysis of Cellulose to Prepare Levoglucosenone Using Sulfated Zirconia
Author(s) -
Wang Zhi,
Lu Qiang,
Zhu XiFeng,
Zhang Ying
Publication year - 2011
Publication title -
chemsuschem
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 2.412
H-Index - 157
eISSN - 1864-564X
pISSN - 1864-5631
DOI - 10.1002/cssc.201000210
Subject(s) - cellulose , catalysis , calcination , yield (engineering) , pyrolysis , cubic zirconia , leaching (pedology) , selectivity , chemistry , sulfation , desorption , nuclear chemistry , adsorption , organic chemistry , chemical engineering , materials science , ceramic , composite material , biochemistry , environmental science , soil science , engineering , soil water
Sulfated zirconia was employed as catalyst for fast pyrolysis of cellulose to prepare levoglucosenone (LGO), a very important anhydrosugar for organic synthesis. The yield and the selectivity of LGO were studied in a fixed‐bed reactor at different temperatures and cellulose/catalyst mass ratios. The experiments of catalyst recycling were also carried out. The results displayed that from 290 to 400 °C, the liquid and solid accounted for more than 95 wt % of products, and the higher temperature led to more liquid and less solid products. The introduction of SO 4 2− /ZrO 2 could promote cellulose conversion and LGO production. The temperature had a similar effect on the yield and selectivity of LGO at different cellulose/catalyst mass ratios. The maximum yield was obtained at 335 °C. Although the structure of the parent ZrO 2 was retained after recycles, which was confirmed by X‐ray diffraction and N 2 adsorption–desorption measurements, the activity of SO 4 2− /ZrO 2 could only be partially recovered by simply calcination. The catalytic activity decrease could be mainly attributed to SO 4 2− leaching, and the activity could be restored by further impregnation of H 2 SO 4 .