Hydrodeoxygenation of Phenol as a Model Compound by Ni2P/HBeta-SBA-15

The stable silica sieve-based HBeta-SBA-15 catalyst-carrier was successfully prepared by a hydrothermal synthesis method, and then Ni2P/HBeta-SBA-15 new hydrodeoxygenation catalyst was successfully loaded by the equal volume impregnation method. It was characterized by X-ray diffraction (XRD), N2 ad...

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Main Authors: Jiao Jiang, Shurong Wang, Jin Li, Yang Cao, Shiyun Zhou, Mingyuan Gao, Boheng Tang
Format: Article
Language:English
Published: North Carolina State University 2023-06-01
Series:BioResources
Subjects:
Online Access:https://ojs.cnr.ncsu.edu/index.php/BRJ/article/view/22584
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author Jiao Jiang
Shurong Wang
Jin Li
Yang Cao
Shiyun Zhou
Mingyuan Gao
Boheng Tang
author_facet Jiao Jiang
Shurong Wang
Jin Li
Yang Cao
Shiyun Zhou
Mingyuan Gao
Boheng Tang
author_sort Jiao Jiang
collection DOAJ
description The stable silica sieve-based HBeta-SBA-15 catalyst-carrier was successfully prepared by a hydrothermal synthesis method, and then Ni2P/HBeta-SBA-15 new hydrodeoxygenation catalyst was successfully loaded by the equal volume impregnation method. It was characterized by X-ray diffraction (XRD), N2 adsorption-desorption, scanning electron microscopy (SEM), transmission electron microscopy (TEM), and pyrolysis-infrared (Py-IR) methods. The results showed that SBA-15 was successfully immobilized on HBeta to form a microporous and mesoporous composite carrier. The introduction of SBA-15 not only increased the specific surface area of HBeta-SBA-15, but also reduced its acidity. After loading the active metal component Ni2P, the structure of the catalyst has not changed much. Hydrodeoxygenation (HDO) of phenol model compounds over Ni2P/HBeta-SBA-15 catalyst was studied in water. The response surface analysis showed that the conversion of phenol was 84.4% and the selectivity of cyclohexane was 94.2% at a lower temperature of 240 °C. The effect of reaction conditions on the yield of cyclohexane was as follows: the reaction temperature > the amount of hydrogen > the amount of catalyst > the reaction time. This study provides theoretical guidance for upgrading biomass pyrolysis oil to green fuel through hydrodeoxygenation.
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spelling doaj.art-4b6fec319ea74030aa0f42063e057adb2023-07-07T18:51:58ZengNorth Carolina State UniversityBioResources1930-21262023-06-0118351655181612Hydrodeoxygenation of Phenol as a Model Compound by Ni2P/HBeta-SBA-15Jiao Jiang0Shurong Wang1Jin Li2Yang Cao3Shiyun Zhou4Mingyuan Gao5Boheng Tang6College of Chemical Engineering and Technology, Hainan University, Haikou 570228, Hainan, ChinaCollege of Chemical Engineering and Technology, Hainan University, Haikou 570228, Hainan, ChinaCollege of Chemical Engineering and Technology, Hainan University, Haikou 570228, Hainan, ChinaHainan University, Haikou 570228, Hainan, ChinaCollege of Chemical Engineering and Technology, Hainan University, Haikou 570228, Hainan, ChinaCollege of Chemical Engineering and Technology, Hainan University, Haikou 570228, Hainan, ChinaCollege of Chemical Engineering and Technology, Hainan University, Haikou 570228, Hainan, ChinaThe stable silica sieve-based HBeta-SBA-15 catalyst-carrier was successfully prepared by a hydrothermal synthesis method, and then Ni2P/HBeta-SBA-15 new hydrodeoxygenation catalyst was successfully loaded by the equal volume impregnation method. It was characterized by X-ray diffraction (XRD), N2 adsorption-desorption, scanning electron microscopy (SEM), transmission electron microscopy (TEM), and pyrolysis-infrared (Py-IR) methods. The results showed that SBA-15 was successfully immobilized on HBeta to form a microporous and mesoporous composite carrier. The introduction of SBA-15 not only increased the specific surface area of HBeta-SBA-15, but also reduced its acidity. After loading the active metal component Ni2P, the structure of the catalyst has not changed much. Hydrodeoxygenation (HDO) of phenol model compounds over Ni2P/HBeta-SBA-15 catalyst was studied in water. The response surface analysis showed that the conversion of phenol was 84.4% and the selectivity of cyclohexane was 94.2% at a lower temperature of 240 °C. The effect of reaction conditions on the yield of cyclohexane was as follows: the reaction temperature > the amount of hydrogen > the amount of catalyst > the reaction time. This study provides theoretical guidance for upgrading biomass pyrolysis oil to green fuel through hydrodeoxygenation.https://ojs.cnr.ncsu.edu/index.php/BRJ/article/view/22584phenol ni2p/hbeta-sba-15response surface methodhydrodeoxidation
spellingShingle Jiao Jiang
Shurong Wang
Jin Li
Yang Cao
Shiyun Zhou
Mingyuan Gao
Boheng Tang
Hydrodeoxygenation of Phenol as a Model Compound by Ni2P/HBeta-SBA-15
BioResources
phenol
ni2p/hbeta-sba-15
response surface method
hydrodeoxidation
title Hydrodeoxygenation of Phenol as a Model Compound by Ni2P/HBeta-SBA-15
title_full Hydrodeoxygenation of Phenol as a Model Compound by Ni2P/HBeta-SBA-15
title_fullStr Hydrodeoxygenation of Phenol as a Model Compound by Ni2P/HBeta-SBA-15
title_full_unstemmed Hydrodeoxygenation of Phenol as a Model Compound by Ni2P/HBeta-SBA-15
title_short Hydrodeoxygenation of Phenol as a Model Compound by Ni2P/HBeta-SBA-15
title_sort hydrodeoxygenation of phenol as a model compound by ni2p hbeta sba 15
topic phenol
ni2p/hbeta-sba-15
response surface method
hydrodeoxidation
url https://ojs.cnr.ncsu.edu/index.php/BRJ/article/view/22584
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