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Bio-oil from fast pyrolysis of lignin: Effects of process and upgrading parameters

Journal

BIORESOURCE TECHNOLOGY
Volume 241, Issue -, Pages 1118-1126

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.biortech.2017.05.129

Keywords

Lignin pyrolysis; Bio-oil; Process parameters; Upgrading

Funding

  1. International Science and Technology Cooperation Program of China [2014DFA61040]
  2. Program of Natural Science Foundation of China [21466022]
  3. Key project of Jiangxi Provincial Department of Science and Technology [20161BBF60057, GCXZ2014-124]
  4. Minnesota Environment and Natural Resources Trust Fund
  5. Xcel Energy's Renewable Development Fund
  6. Center for Biorefining

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Effects of process parameters on the yield and chemical profile of bio-oil from fast pyrolysis of lignin and the processes for lignin-derived bio-oil upgrading were reviewed. Various process parameters including pyrolysis temperature, reactor types, lignin characteristics, residence time, and feeding rate were discussed and the optimal parameter conditions for improved bio-oil yield and quality were concluded. In terms of lignin-derived bio-oil upgrading, three routes including pretreatment of lignin, catalytic upgrading, and co-pyrolysis of hydrogen-rich materials have been investigated. Zeolite cracking and hydrodeoxygenation (HDO) treatment are two main methods for catalytic upgrading of lignin-derived bio-oil. Factors affecting zeolite activity and the main zeolite catalytic mechanisms for lignin conversion were analyzed. Noble metal-based catalysts and metal sulfide catalysts are normally used as the HDO catalysts and the conversion mechanisms associated with a series of reactions have been proposed. (C) 2017 Elsevier Ltd. All rights reserved.

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