Catalytic technique of lignin derived bio–oil conversion, has been studied over Pt–γAl2O3 catalyst in a fixed–bed tubular micro–activity flow reactor at 673 K, 14 bar and space velocity 3 (g of Anisole)/(g of catalyst × h), in the presence of H2. A reaction network according to selectivity–conversion data is proposed to describe the evolution of products observed. The reactions include the following, anisole to benzene via HDO, to hexamethylbenzene via hydrodeoxygenation and alkylation, to phenol via hydrogenolysis, to 2–methylphenol via transalkylation and finally to 2, 4–dimethylphenol, 2, 4, 6–trimethylphenol and 2, 3, 5, 6–tetramethylphenol via transalkylation and alkylation. Experimental results indicated that the anisole conversion decreases about 20% with increasing the pressure from 8 to 14 bar at 673 K.
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American Journal of Chemical Engineering (Volume 5, Issue 2-1)
This article belongs to the Special Issue Advanced Chemical and Biochemical Technology for Biofuels |
DOI | 10.11648/j.ajche.s.2017050201.11 |
Page(s) | 1-5 |
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This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
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Copyright © The Author(s), 2017. Published by Science Publishing Group |
Bio−oil, Valuable Chemicals, Anisole, Catalytic Conversion, Hydrodeoxygenation
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APA Style
Majid Saidi. (2017). Catalytic Technique of Bio–oil Conversion to Valuable Chemicals. American Journal of Chemical Engineering, 5(2-1), 1-5. https://doi.org/10.11648/j.ajche.s.2017050201.11
ACS Style
Majid Saidi. Catalytic Technique of Bio–oil Conversion to Valuable Chemicals. Am. J. Chem. Eng. 2017, 5(2-1), 1-5. doi: 10.11648/j.ajche.s.2017050201.11
@article{10.11648/j.ajche.s.2017050201.11, author = {Majid Saidi}, title = {Catalytic Technique of Bio–oil Conversion to Valuable Chemicals}, journal = {American Journal of Chemical Engineering}, volume = {5}, number = {2-1}, pages = {1-5}, doi = {10.11648/j.ajche.s.2017050201.11}, url = {https://doi.org/10.11648/j.ajche.s.2017050201.11}, eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.s.2017050201.11}, abstract = {Catalytic technique of lignin derived bio–oil conversion, has been studied over Pt–γAl2O3 catalyst in a fixed–bed tubular micro–activity flow reactor at 673 K, 14 bar and space velocity 3 (g of Anisole)/(g of catalyst × h), in the presence of H2. A reaction network according to selectivity–conversion data is proposed to describe the evolution of products observed. The reactions include the following, anisole to benzene via HDO, to hexamethylbenzene via hydrodeoxygenation and alkylation, to phenol via hydrogenolysis, to 2–methylphenol via transalkylation and finally to 2, 4–dimethylphenol, 2, 4, 6–trimethylphenol and 2, 3, 5, 6–tetramethylphenol via transalkylation and alkylation. Experimental results indicated that the anisole conversion decreases about 20% with increasing the pressure from 8 to 14 bar at 673 K.}, year = {2017} }
TY - JOUR T1 - Catalytic Technique of Bio–oil Conversion to Valuable Chemicals AU - Majid Saidi Y1 - 2017/02/28 PY - 2017 N1 - https://doi.org/10.11648/j.ajche.s.2017050201.11 DO - 10.11648/j.ajche.s.2017050201.11 T2 - American Journal of Chemical Engineering JF - American Journal of Chemical Engineering JO - American Journal of Chemical Engineering SP - 1 EP - 5 PB - Science Publishing Group SN - 2330-8613 UR - https://doi.org/10.11648/j.ajche.s.2017050201.11 AB - Catalytic technique of lignin derived bio–oil conversion, has been studied over Pt–γAl2O3 catalyst in a fixed–bed tubular micro–activity flow reactor at 673 K, 14 bar and space velocity 3 (g of Anisole)/(g of catalyst × h), in the presence of H2. A reaction network according to selectivity–conversion data is proposed to describe the evolution of products observed. The reactions include the following, anisole to benzene via HDO, to hexamethylbenzene via hydrodeoxygenation and alkylation, to phenol via hydrogenolysis, to 2–methylphenol via transalkylation and finally to 2, 4–dimethylphenol, 2, 4, 6–trimethylphenol and 2, 3, 5, 6–tetramethylphenol via transalkylation and alkylation. Experimental results indicated that the anisole conversion decreases about 20% with increasing the pressure from 8 to 14 bar at 673 K. VL - 5 IS - 2-1 ER -