Journal
ENERGY CONVERSION AND MANAGEMENT
Volume 236, Issue -, Pages -Publisher
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.enconman.2021.114020
Keywords
Hierarchical zeolite; Re-assembly; Lignin; Co-pyrolysis; Aromatics
Categories
Funding
- Agriculture and Food Research Initiative Competitive Grant from the National Institute of Food and Agriculture, United States Department of Agriculture [2016-67021-24533, 2018-67009-27904]
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Biomass-derived materials have great potential as an alternative templating agent for tailoring new pore systems in zeolites to enhance catalyst properties. In this study, hierarchical ZSM-5 was prepared with the assistance of alkaline lignin and showed improved catalytic performance in co-pyrolysis of softwood biomass and LDPE mixture. The enlarged pore openings in hierarchical ZSM-5 facilitated the passage of reactive species and resulted in higher selectivity of desirable aromatic hydrocarbons and coke formation inhibition compared to parent zeolite.
Biomass-derived materials offer a huge potential as an alternative templating agent for tailoring new pore systems in zeolite to enhance its catalyst properties. Hierarchical ZSM-5 (H-type) was prepared in this study with the assistance of alkaline lignin in the re-assembly of alkali-treated parent material. The catalytic performance of the novel zeolite was tested in catalytic co-pyrolysis of softwood biomass and LDPE mixture, and the product distribution was optimized with varying reaction temperature (?C) and plastic loading (g/g biomass). Results suggested that the enlarged pore openings in hierarchical ZSM-5 facilitated abundant reactive species, including the macromolecule oxygenates derived from lignin fraction in softwood, and deoxygenated products to pass through the catalyst layer. The higher selectivity of desirable aromatic hydrocarbons as well as coke formation inhibition were obtained at 450 ?C compared to parent zeolite. Thus, the synergy of LDPE blending was intensified in hierarchical ZSM-5 through acid-catalyzed cracking and aromatization during catalytic upgrading.
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