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Production of phenols from lignin via depolymerization and catalytic cracking
Production of phenols from lignin was investigated using a new conversion process consisting of two reaction steps. In the first step, depolymerization of lignin was carried out in an autoclave reactor using a silica-alumina catalyst in a water/1-butanol solution. The yield of lignin-derived liquid...
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Published in: | Fuel processing technology 2013-04, Vol.108, p.69-75 |
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Main Authors: | , , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | Production of phenols from lignin was investigated using a new conversion process consisting of two reaction steps. In the first step, depolymerization of lignin was carried out in an autoclave reactor using a silica-alumina catalyst in a water/1-butanol solution. The yield of lignin-derived liquid product reached 85–88C-mol% under the appropriate reaction conditions. In the second step, catalytic cracking of the liquid products from the first step was carried out using a fixed‐bed flow reactor over an iron oxide catalyst. With this method, total recovered fraction of phenols and the conversion of methoxy phenol reached 6.6–8.6% and 92–94%, respectively.
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► Production of phenols from lignin was investigated via a two-step process. ► Depolymerization of lignin over silica-alumina was promoted using a H2O/BuOH solution. ► Reaction of the lignin-derived liquid product was carried out over an iron oxide catalyst. ► The iron oxide catalyst successfully converted phenols into phenol and cresol. |
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ISSN: | 0378-3820 1873-7188 |
DOI: | 10.1016/j.fuproc.2012.05.003 |