Chem. J. Chinese Universities ›› 2018, Vol. 39 ›› Issue (4): 735.doi: 10.7503/cjcu20170591

• Physical Chemistry • Previous Articles     Next Articles

Depolymerization of the Alkali Lignin for Aromatic Compounds over Ni/SiO2-Al2O3 Solid Acid Catalysts

ZHOU Lie1,2, WU Qingyun2, XU Ying2,*(), WANG Chenguang2, MA Longlong2, LI Wenzhi1, CHEN Peili2   

  1. 1. Nano Science and Technology Institute, University of Science and Technology of China, Suzhou 215123, China
    2. Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, CAS Key Laboratory of Renewable Energy,Guangdong Provincial Key Laboratory of New and Renewable Energy Research and Development,Guangzhou 510640, China
  • Received:2017-08-31 Online:2018-04-10 Published:2018-03-27
  • Contact: XU Ying E-mail:xuying@ms.giec.ac.cn
  • Supported by:
    † Supported by the National Natural Science Foundationof China(No.51676191), the Youth Science and Technology Innovation Talents Plan of Guangdong Province, China(No.2015TQ01W652), the Science and Technology Plan Project of Guangdong Province, China(No.2014A010106019), the Program of Youth Innovation Promotion Association of Chinese Academy of Sciences(No.2016313)

Abstract:

Optional discarded and unreasonable utilization of industrial alkali lignin leaded to water and air pollution. However, alkali lignin could be utilized as fine chemical resource for its specific phenyl propane structure. In this paper, we investigated efficient depolymerization methods on alkali lignin aiming for aromatic products over acidic SiO2-Al2O3 and Ni/SiO2-Al2O3 by one-step. The effects of Ni metal loading contents, reaction temperature and reaction time in this process were also discussed. Analysis of lignin depolymerized products were carried with gas chromatography(GC), gas chromatography-mass spectrometry(GC-MS), Fourier transform-infrared spectroscopy(FTIR). The results showed that Ni/SiO2-Al2O3 can promote the conversion of the alkali lignin. Yield(mass fraction) of aromatic products increased and then decreased along with the rising of reaction temperature, which the yield of arenes was 9.05% and the yield of aromatic products was 22.53% over 15%Ni/SiO2-Al2O3 catalyst at 300 ℃ after depolymerization. Reaction time also showed significantly influence on depolymerized products, with the reaction times increasing. The arenes yield was increased and then stabilized, aromatic products yield reached 26.54% after reacted 12 h.

Key words: Ni catalyst, Alkali Lignin, Hydrogenolysis, Aromatics

CLC Number: 

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