Study on biomass adsorption‐enhanced steam gasification for hydrogen production based on dual‐effect catalyst

Abstract In this study, in order to achieve CO 2 capture under high‐temperature conditions and obtain hydrogen from biomass, a dual‐effect catalyst Ni( x )‐Na 2 ZrO 3 , possessing both catalytic and high‐temperature CO 2 adsorption capabilities, was prepared and applied in the biomass steam reforming reaction. The investigation focused on the impact of gasification temperature, steam to carbon (S/C) ratio, and Ni loading ratio on the production of hydrogen‐rich syngas via biomass enhanced steam gasification over the catalysts. By thermogravimetric analysis, the catalyst exhibited a remarkable high‐temperature CO 2 adsorption capability at 900°C and cyclic stability. The orthogonal experiment was conducted for the reaction characteristics of the biomass adsorption‐enhanced steam gasification over the dual‐effect Ni( x )‐Na 2 ZrO 3 catalyst. Through the analysis of the fitting formula, the catalyst successfully demonstrated promotional effect on the biomass reforming reaction. When the gasification temperature was 950°C, S/C ratio was 9 and Ni loading ratio was 7.7 wt%, the hydrogen yield reached 0.95 m 3 /kg, and carbon deposition rate was almost 0.

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Publication Details

Journal
Environmental Progress & Sustainable Energy
Published
2025-02-03
DOI
https://doi.org/10.1002/ep.14566
Citations
1
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
0.67

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Study on biomass adsorption‐enhanced steam gasification for hydrogen production based on dual‐effect catalyst

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article

Study on biomass adsorption‐enhanced steam gasification for hydrogen production based on dual‐effect catalyst

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article en
1 citations

Abstract

Abstract In this study, in order to achieve CO 2 capture under high‐temperature conditions and obtain hydrogen from biomass, a dual‐effect catalyst Ni( x )‐Na 2 ZrO 3 , possessing both catalytic and high‐temperature CO 2 adsorption capabilities, was prepared and applied in the biomass steam reforming reaction. The investigation focused on the impact of gasification temperature, steam to carbon (S/C) ratio, and Ni loading ratio on the production of hydrogen‐rich syngas via biomass enhanced steam gasification over the catalysts. By thermogravimetric analysis, the catalyst exhibited a remarkable high‐temperature CO 2 adsorption capability at 900°C and cyclic stability. The orthogonal experiment was conducted for the reaction characteristics of the biomass adsorption‐enhanced steam gasification over the dual‐effect Ni( x )‐Na 2 ZrO 3 catalyst. Through the analysis of the fitting formula, the catalyst successfully demonstrated promotional effect on the biomass reforming reaction. When the gasification temperature was 950°C, S/C ratio was 9 and Ni loading ratio was 7.7 wt%, the hydrogen yield reached 0.95 m 3 /kg, and carbon deposition rate was almost 0.

Environmental Progress & Sustainable EnergyVol. 44(2)
Northeastern University (CN)
National Natural Science Foundation of China, Higher Education Discipline Innovation Project
Openalex Percentile: Top 35%
Thermochemical Biomass Conversion Processes
0.67
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