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Upgrading of Light Bio-oil from Solvothermolysis Liquefaction of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation Using NiMo/Al(2)O(3) or CoMo/Al(2)O(3) Catalysts
[Image: see text] Hydrodeoxygenation (HDO) of bio-oil derived from liquefaction of a palm empty fruit bunch (EFB) in glycerol was investigated. To enhance the heating value and reduce the oxygen content of upgraded bio-oil, hydrodeoxygenation of light bio-oil over Ni- and Co-based catalysts on an Al...
Autores principales: | , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
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American Chemical Society
2021
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7860089/ https://www.ncbi.nlm.nih.gov/pubmed/33553918 http://dx.doi.org/10.1021/acsomega.0c05387 |
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author | Muangsuwan, Chutanan Kriprasertkul, Warangthat Ratchahat, Sakhon Liu, Chen-Guang Posoknistakul, Pattaraporn Laosiripojana, Navadol Sakdaronnarong, Chularat |
author_facet | Muangsuwan, Chutanan Kriprasertkul, Warangthat Ratchahat, Sakhon Liu, Chen-Guang Posoknistakul, Pattaraporn Laosiripojana, Navadol Sakdaronnarong, Chularat |
author_sort | Muangsuwan, Chutanan |
collection | PubMed |
description | [Image: see text] Hydrodeoxygenation (HDO) of bio-oil derived from liquefaction of a palm empty fruit bunch (EFB) in glycerol was investigated. To enhance the heating value and reduce the oxygen content of upgraded bio-oil, hydrodeoxygenation of light bio-oil over Ni- and Co-based catalysts on an Al(2)O(3) support was performed in a rotating-bed reactor. Two consecutive steps were conducted to produce bio-oil from EFB including (1) microwave-assisted wet torrefaction of EFB and (2) solvothermolysis liquefaction of treated EFB in a Na(2)CO(3)/glycerol system. The HDO of as-prepared bio-oil was subsequently performed in a unique design reactor possessing a rotating catalyst bed for efficient interaction of a catalyst with bio-oil and facile separation of the catalyst from upgraded bio-oil after the reaction. The reaction was carried out in the presence of each mono- or bimetallic catalyst, namely, Co/Al(2)O(3), Ni/Al(2)O(3), NiMo/Al(2)O(3), and CoMo/Al(2)O(3), packed in the rotating-mesh host with a rotation speed of 250 rpm and kept at 300 and 350 °C, 2 MPa hydrogen for 1 h. From the results, the qualities of upgraded bio-oil were substantially improved for all catalysts tested in terms of oxygen reduction and increased high heating value (HHV). Particularly, the NiMo/Al(2)O(3) catalyst exhibited the most promising catalyst, providing favorable bio-oil yield and HHV. Remarkably greater energy ratios and carbon recovery together with high H/O, C/O, and H/C ratios were additionally achieved from the NiMo/Al(2)O(3) catalyst compared with other catalysts. Cyclopentanone and cyclopentene were the main olefins found in hydrodeoxygenated bio-oil derived from liquefied EFB. It was observed that cyclopentene was first generated and subsequently converted to cyclopentanone under the hydrogenation reaction. These compounds can be further used as a building block in the synthesis of jet-fuel range cycloalkanes. |
format | Online Article Text |
id | pubmed-7860089 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2021 |
publisher | American Chemical Society |
record_format | MEDLINE/PubMed |
spelling | pubmed-78600892021-02-05 Upgrading of Light Bio-oil from Solvothermolysis Liquefaction of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation Using NiMo/Al(2)O(3) or CoMo/Al(2)O(3) Catalysts Muangsuwan, Chutanan Kriprasertkul, Warangthat Ratchahat, Sakhon Liu, Chen-Guang Posoknistakul, Pattaraporn Laosiripojana, Navadol Sakdaronnarong, Chularat ACS Omega [Image: see text] Hydrodeoxygenation (HDO) of bio-oil derived from liquefaction of a palm empty fruit bunch (EFB) in glycerol was investigated. To enhance the heating value and reduce the oxygen content of upgraded bio-oil, hydrodeoxygenation of light bio-oil over Ni- and Co-based catalysts on an Al(2)O(3) support was performed in a rotating-bed reactor. Two consecutive steps were conducted to produce bio-oil from EFB including (1) microwave-assisted wet torrefaction of EFB and (2) solvothermolysis liquefaction of treated EFB in a Na(2)CO(3)/glycerol system. The HDO of as-prepared bio-oil was subsequently performed in a unique design reactor possessing a rotating catalyst bed for efficient interaction of a catalyst with bio-oil and facile separation of the catalyst from upgraded bio-oil after the reaction. The reaction was carried out in the presence of each mono- or bimetallic catalyst, namely, Co/Al(2)O(3), Ni/Al(2)O(3), NiMo/Al(2)O(3), and CoMo/Al(2)O(3), packed in the rotating-mesh host with a rotation speed of 250 rpm and kept at 300 and 350 °C, 2 MPa hydrogen for 1 h. From the results, the qualities of upgraded bio-oil were substantially improved for all catalysts tested in terms of oxygen reduction and increased high heating value (HHV). Particularly, the NiMo/Al(2)O(3) catalyst exhibited the most promising catalyst, providing favorable bio-oil yield and HHV. Remarkably greater energy ratios and carbon recovery together with high H/O, C/O, and H/C ratios were additionally achieved from the NiMo/Al(2)O(3) catalyst compared with other catalysts. Cyclopentanone and cyclopentene were the main olefins found in hydrodeoxygenated bio-oil derived from liquefied EFB. It was observed that cyclopentene was first generated and subsequently converted to cyclopentanone under the hydrogenation reaction. These compounds can be further used as a building block in the synthesis of jet-fuel range cycloalkanes. American Chemical Society 2021-01-21 /pmc/articles/PMC7860089/ /pubmed/33553918 http://dx.doi.org/10.1021/acsomega.0c05387 Text en © 2021 The Authors. Published by American Chemical Society This is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License (http://pubs.acs.org/page/policy/authorchoice_ccbyncnd_termsofuse.html) , which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes. |
spellingShingle | Muangsuwan, Chutanan Kriprasertkul, Warangthat Ratchahat, Sakhon Liu, Chen-Guang Posoknistakul, Pattaraporn Laosiripojana, Navadol Sakdaronnarong, Chularat Upgrading of Light Bio-oil from Solvothermolysis Liquefaction of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation Using NiMo/Al(2)O(3) or CoMo/Al(2)O(3) Catalysts |
title | Upgrading of Light Bio-oil from Solvothermolysis Liquefaction
of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation
Using NiMo/Al(2)O(3) or CoMo/Al(2)O(3) Catalysts |
title_full | Upgrading of Light Bio-oil from Solvothermolysis Liquefaction
of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation
Using NiMo/Al(2)O(3) or CoMo/Al(2)O(3) Catalysts |
title_fullStr | Upgrading of Light Bio-oil from Solvothermolysis Liquefaction
of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation
Using NiMo/Al(2)O(3) or CoMo/Al(2)O(3) Catalysts |
title_full_unstemmed | Upgrading of Light Bio-oil from Solvothermolysis Liquefaction
of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation
Using NiMo/Al(2)O(3) or CoMo/Al(2)O(3) Catalysts |
title_short | Upgrading of Light Bio-oil from Solvothermolysis Liquefaction
of an Oil Palm Empty Fruit Bunch in Glycerol by Catalytic Hydrodeoxygenation
Using NiMo/Al(2)O(3) or CoMo/Al(2)O(3) Catalysts |
title_sort | upgrading of light bio-oil from solvothermolysis liquefaction
of an oil palm empty fruit bunch in glycerol by catalytic hydrodeoxygenation
using nimo/al(2)o(3) or como/al(2)o(3) catalysts |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7860089/ https://www.ncbi.nlm.nih.gov/pubmed/33553918 http://dx.doi.org/10.1021/acsomega.0c05387 |
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