Development of a fluidized bed reactor for catalytic dry reforming of methane with CO2

• A pilot fluidized bed reactor (FBR) was developed with fluidization behaviors analyzed. • The FBR was used to conduct catalytic dry reforming of methane (DRM) with CO 2 . • Practical nickel supported on FCC particles (Ni/FCC) was prepared for DRM in FBR. • Systematic experimental studies of catalytic DRM in FBR. • Comparison of catalytic performance of DRM in FBR and a packed bed reactor. Experimental studies of dry reforming of methane (DRM) under bubbling regime in the thermal fluidized bed reactors (FBRs) remain limited. In this study, a thermal FBR was developed, and catalytic DRM was systematically evaluated. Nickel-supported catalysts (Ni/FCC) were prepared via a wet impregnation method using commercial fluid catalytic cracking (FCC) particles, and their physicochemical properties were comprehensively characterized. Detailed fluidization behaviour was investigated using pressure drop fluctuations and discrete wavelet transformation (DWT), revealing a transition velocity (Uc) between bubbling and turbulent regimes in the FBR (under the conditions relevant to DRM), which was found to decrease with increasing temperature. DRM performance of Ni/FCC was assessed under various reaction temperatures (600–800 °C), gas velocities (0.1–0.2 m/s), and preheating conditions. Optimal operation in the bubbling regime (800 °C, 0.1 m/s) enabled CO 2 and CH 4 conversions of 57% and 41%, respectively, with an H 2 /CO ratio of 0.67. Comparative studies demonstrated that the packed bed reactor (PBR) achieved higher conversions and better H 2 /CO ratios (∼0.96), attributed to its plug flow characteristics, whereas the FBR exhibited lower conversions due to gas back mixing and reactant bypassing. Nevertheless, the Ni/FCC catalyst exhibited good thermal stability and negligible deactivation in both reactor configurations during 20 h of continuous operation. These findings provide practical insights into the design, operation, and catalytic behaviour of FBR systems for industrial DRM applications.

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Publication Details

Journal
Carbon Capture Science & Technology
Published
2025-11-16
DOI
https://doi.org/10.1016/j.ccst.2025.100540
Primary Topic
Catalysts for Methane Reforming
Type
article
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article

Development of a fluidized bed reactor for catalytic dry reforming of methane with CO2

Xiaolei Fan, Huanhao Chen, Rongsheng Cai, Li Lyu et al.
Carbon Capture Science & Technology
Catalysts for Methane Reforming
article

Development of a fluidized bed reactor for catalytic dry reforming of methane with CO2

Xiaolei Fan, Huanhao Chen, Rongsheng Cai, Li Lyu, Yilai Jiao, Xiaoxia Ou, Lifeng Xiao, Shihang Yu, Cong Li, Xiaoyang Wei
article en

Abstract

• A pilot fluidized bed reactor (FBR) was developed with fluidization behaviors analyzed. • The FBR was used to conduct catalytic dry reforming of methane (DRM) with CO 2 . • Practical nickel supported on FCC particles (Ni/FCC) was prepared for DRM in FBR. • Systematic experimental studies of catalytic DRM in FBR. • Comparison of catalytic performance of DRM in FBR and a packed bed reactor. Experimental studies of dry reforming of methane (DRM) under bubbling regime in the thermal fluidized bed reactors (FBRs) remain limited. In this study, a thermal FBR was developed, and catalytic DRM was systematically evaluated. Nickel-supported catalysts (Ni/FCC) were prepared via a wet impregnation method using commercial fluid catalytic cracking (FCC) particles, and their physicochemical properties were comprehensively characterized. Detailed fluidization behaviour was investigated using pressure drop fluctuations and discrete wavelet transformation (DWT), revealing a transition velocity (Uc) between bubbling and turbulent regimes in the FBR (under the conditions relevant to DRM), which was found to decrease with increasing temperature. DRM performance of Ni/FCC was assessed under various reaction temperatures (600–800 °C), gas velocities (0.1–0.2 m/s), and preheating conditions. Optimal operation in the bubbling regime (800 °C, 0.1 m/s) enabled CO 2 and CH 4 conversions of 57% and 41%, respectively, with an H 2 /CO ratio of 0.67. Comparative studies demonstrated that the packed bed reactor (PBR) achieved higher conversions and better H 2 /CO ratios (∼0.96), attributed to its plug flow characteristics, whereas the FBR exhibited lower conversions due to gas back mixing and reactant bypassing. Nevertheless, the Ni/FCC catalyst exhibited good thermal stability and negligible deactivation in both reactor configurations during 20 h of continuous operation. These findings provide practical insights into the design, operation, and catalytic behaviour of FBR systems for industrial DRM applications.

Carbon Capture Science & TechnologyVol. 17
University of Science and Technology of China (CN), Nanjing Tech University (CN), University of Nottingham Ningbo China (CN), Chinese Academy of Sciences (CN), University of Manchester (GB), Lanzhou Institute of Chemical Physics (CN)
Openalex Percentile: Top 79%
Catalysts for Methane Reforming
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