Aqueous-Phase Reforming of Biogas Slurry over MOF-Derived α-MoO<sub>3</sub> Catalyst for Producing Renewable Hydrogen: Effect of Fermenting Time

Aqueous-phase reforming (APR) is an alternative method for treating and utilizing biogas slurry (BS) to produce renewable hydrogen from organic oxygen-containing wastewater. Considering the fluctuating characteristics of BS with changes in the degree of fermentation, developing an efficient catalyst...

Full description

Saved in:
Bibliographic Details
Main Authors: Qingguo Bu, Jian Wang, Yuxuan Chen, Junyu Tao, Akash Kumar, Beibei Yan, Guanyi Chen
Format: Article
Language:English
Published: MDPI AG 2024-11-01
Series:Molecules
Subjects:
Online Access:https://www.mdpi.com/1420-3049/29/23/5565
Tags: Add Tag
No Tags, Be the first to tag this record!
_version_ 1846124046059569152
author Qingguo Bu
Jian Wang
Yuxuan Chen
Junyu Tao
Akash Kumar
Beibei Yan
Guanyi Chen
author_facet Qingguo Bu
Jian Wang
Yuxuan Chen
Junyu Tao
Akash Kumar
Beibei Yan
Guanyi Chen
author_sort Qingguo Bu
collection DOAJ
description Aqueous-phase reforming (APR) is an alternative method for treating and utilizing biogas slurry (BS) to produce renewable hydrogen from organic oxygen-containing wastewater. Considering the fluctuating characteristics of BS with changes in the degree of fermentation, developing an efficient catalyst is a major concern for the APR of BS. The novel catalyst based on molybdenum-based metal–organic-framework-derived oxides (Mo-MOF-derived α-MoO<sub>3</sub>) was reported in this study. The results indicated that the variables (e.g., pH, organic load, and salinity) of BS corresponded to the fermentation times and exhibited decreasing trends after APR under the reaction conditions of 225 °C and 30 min. Decarboxylation was identified as the main side reaction in the APR of BS over the catalyst. An optimal yield of 2.17 mL<sub>hydrogen</sub>/mL<sub>BS</sub> was achieved when BS was obtained from 6 days of fermentation. Finally, the Mo-MOF-derived α-MoO<sub>3</sub> catalyst was obtained from the greater specific surface area of MOFs. The catalyst had a weaker acidity than the initial α-MoO<sub>3</sub>, making it more preferred for facilitating the APR of BS.
format Article
id doaj-art-1dcb2d0ed8fb4853a8540ca03fe923dd
institution Kabale University
issn 1420-3049
language English
publishDate 2024-11-01
publisher MDPI AG
record_format Article
series Molecules
spelling doaj-art-1dcb2d0ed8fb4853a8540ca03fe923dd2024-12-13T16:28:18ZengMDPI AGMolecules1420-30492024-11-012923556510.3390/molecules29235565Aqueous-Phase Reforming of Biogas Slurry over MOF-Derived α-MoO<sub>3</sub> Catalyst for Producing Renewable Hydrogen: Effect of Fermenting TimeQingguo Bu0Jian Wang1Yuxuan Chen2Junyu Tao3Akash Kumar4Beibei Yan5Guanyi Chen6School of Environmental Science and Engineering, Tianjin University, Tianjin 300350, ChinaSchool of Energy and Environment, Shenyang Aerospace University, Shenyang 110036, ChinaSchool of Environmental Science and Engineering, Tianjin University, Tianjin 300350, ChinaSchool of Mechanical Engineering, Tianjin University of Commerce, Tianjin 300134, ChinaSchool of Environmental Science and Engineering, Tianjin University, Tianjin 300350, ChinaSchool of Environmental Science and Engineering, Tianjin University, Tianjin 300350, ChinaSchool of Mechanical Engineering, Tianjin University of Commerce, Tianjin 300134, ChinaAqueous-phase reforming (APR) is an alternative method for treating and utilizing biogas slurry (BS) to produce renewable hydrogen from organic oxygen-containing wastewater. Considering the fluctuating characteristics of BS with changes in the degree of fermentation, developing an efficient catalyst is a major concern for the APR of BS. The novel catalyst based on molybdenum-based metal–organic-framework-derived oxides (Mo-MOF-derived α-MoO<sub>3</sub>) was reported in this study. The results indicated that the variables (e.g., pH, organic load, and salinity) of BS corresponded to the fermentation times and exhibited decreasing trends after APR under the reaction conditions of 225 °C and 30 min. Decarboxylation was identified as the main side reaction in the APR of BS over the catalyst. An optimal yield of 2.17 mL<sub>hydrogen</sub>/mL<sub>BS</sub> was achieved when BS was obtained from 6 days of fermentation. Finally, the Mo-MOF-derived α-MoO<sub>3</sub> catalyst was obtained from the greater specific surface area of MOFs. The catalyst had a weaker acidity than the initial α-MoO<sub>3</sub>, making it more preferred for facilitating the APR of BS.https://www.mdpi.com/1420-3049/29/23/5565aqueous-phase reformingMOF derivativesbiogas slurryhydrogenwastewater treatment
spellingShingle Qingguo Bu
Jian Wang
Yuxuan Chen
Junyu Tao
Akash Kumar
Beibei Yan
Guanyi Chen
Aqueous-Phase Reforming of Biogas Slurry over MOF-Derived α-MoO<sub>3</sub> Catalyst for Producing Renewable Hydrogen: Effect of Fermenting Time
Molecules
aqueous-phase reforming
MOF derivatives
biogas slurry
hydrogen
wastewater treatment
title Aqueous-Phase Reforming of Biogas Slurry over MOF-Derived α-MoO<sub>3</sub> Catalyst for Producing Renewable Hydrogen: Effect of Fermenting Time
title_full Aqueous-Phase Reforming of Biogas Slurry over MOF-Derived α-MoO<sub>3</sub> Catalyst for Producing Renewable Hydrogen: Effect of Fermenting Time
title_fullStr Aqueous-Phase Reforming of Biogas Slurry over MOF-Derived α-MoO<sub>3</sub> Catalyst for Producing Renewable Hydrogen: Effect of Fermenting Time
title_full_unstemmed Aqueous-Phase Reforming of Biogas Slurry over MOF-Derived α-MoO<sub>3</sub> Catalyst for Producing Renewable Hydrogen: Effect of Fermenting Time
title_short Aqueous-Phase Reforming of Biogas Slurry over MOF-Derived α-MoO<sub>3</sub> Catalyst for Producing Renewable Hydrogen: Effect of Fermenting Time
title_sort aqueous phase reforming of biogas slurry over mof derived α moo sub 3 sub catalyst for producing renewable hydrogen effect of fermenting time
topic aqueous-phase reforming
MOF derivatives
biogas slurry
hydrogen
wastewater treatment
url https://www.mdpi.com/1420-3049/29/23/5565
work_keys_str_mv AT qingguobu aqueousphasereformingofbiogasslurryovermofderivedamoosub3subcatalystforproducingrenewablehydrogeneffectoffermentingtime
AT jianwang aqueousphasereformingofbiogasslurryovermofderivedamoosub3subcatalystforproducingrenewablehydrogeneffectoffermentingtime
AT yuxuanchen aqueousphasereformingofbiogasslurryovermofderivedamoosub3subcatalystforproducingrenewablehydrogeneffectoffermentingtime
AT junyutao aqueousphasereformingofbiogasslurryovermofderivedamoosub3subcatalystforproducingrenewablehydrogeneffectoffermentingtime
AT akashkumar aqueousphasereformingofbiogasslurryovermofderivedamoosub3subcatalystforproducingrenewablehydrogeneffectoffermentingtime
AT beibeiyan aqueousphasereformingofbiogasslurryovermofderivedamoosub3subcatalystforproducingrenewablehydrogeneffectoffermentingtime
AT guanyichen aqueousphasereformingofbiogasslurryovermofderivedamoosub3subcatalystforproducingrenewablehydrogeneffectoffermentingtime