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Catalytic conversion of particle board over microporous catalysts
Affiliation:1. Graduate school of Energy and Environmental System Engineering, University of Seoul, Seoul 130-743, Republic of Korea;2. Department of Environmental Engineering, Sunchon National University, Suncheon 540-742, Republic of Korea;3. Department of Chemical Engineering, Kongju National University, Cheonan 331-717, Republic of Korea;4. Korea Institute of Energy Research, Daejeon 303-343, Republic of Korea;5. School of Mechanical Engineering, Sungkyunkwan University, Suwon 440-746, Republic of Korea;6. Clean Energy Research Center, Korea Institute of Science and Technology, Seoul 136-791, Republic of Korea;7. School of Environmental Engineering, University of Seoul, Seoul 130-743, Republic of Korea;1. Key Laboratory of Renewable Energy, CAS, Guangdong Key Laboratory of New and Renewable Energy Research and Development, Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangzhou 510640, PR China;2. University of Chinese Academy of Sciences, Beijing 100049, PR China;1. National Renewable Energy Laboratory, 15013 Denver West Parkway, Golden, CO, 80403, USA;2. Colorado State University, Fort Collins, CO, 80523, USA;1. Key Laboratory of Renewable Energy, CAS, Guangdong Provincial Key Laboratory of New and Renewable Energy Research and Development, Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangzhou 510640, China;2. University of Chinese Academy of Sciences, Beijing 100049, China;1. Department of Chemical Technology, Faculty of Science and Center of Excellence on Petrochemical and Materials Technology, Chulalongkorn University, Bangkok, 10330, Thailand;2. Energy Conversion Engineering Laboratory, Institute of Regional Innovation, Hirosaki University, 2-1-3, Matsubara, Aomori, 030-0813, Japan;3. Graduate School of Science and Technology, Hirosaki University, 1-Bunkyocho, Hirosaki, 036-8560, Japan
Abstract:Catalytic pyrolysis of particle board, a type of waste wood that is increasingly produced all over the world, was carried out over three types of zeolite catalysts: HBETA, HZSM-5, and Ga-impregnated HZSM-5 (Ga/HZSM-5). Experiments conducted using a batch reactor showed that the bio-oil yield and gas yield in catalytic pyrolysis were lower and higher than those in non-catalytic pyrolysis, respectively. Analysis of the bio-oil using pyrolysis gas chromatography/mass spectrometry (Py-GC/MS) showed that the yields of high-value-added species such as aromatics and phenolics were increased to a large extent by catalytic upgrading, thus increasing the value of the product bio-oil. In particular, HZSM-5 exhibited high selectivity for aromatic compounds, and impregnation of Ga further increased the selectivity. HBETA could cause levoglucosans to decompose completely owing to its large pore size, resulting in increased yields of low-molecular-mass species.
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