Simultaneous utilization of CO2 and CH4 through dry reforming of methane with Ni–Ce@SiO2 catalyst: Parametric and simulation studies

The dry reforming of methane (DRM) can reduce CO 2 and CH 4 simultaneously. This study utilized East Natuna gas fields, composed of 70 % CO 2 and 30 % CH 4 , for syngas production via DRM using a Ni–Ce@SiO 2 catalyst. The kinetic parameters employed the Langmuir-Hinshelwood mechanism on the surface reaction as the rate-determining step. The simulation results provided an error margin below 5 %. A CO 2 :CH 4 feed ratio of 70:30 at 700 o C achieves higher CH 4 conversion than a 50:50 ratio (97.10 % vs. 79.01 %), yet with lower H 2 /CO ratio (0.68 vs. 0.92). Also, higher temperatures impact shorter reactor lengths and swifter times to reach stable conversion.

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Publication Details

Journal
Case Studies in Chemical and Environmental Engineering
Published
2024-12-18
DOI
https://doi.org/10.1016/j.cscee.2024.101078
Citations
2
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.21

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article

Simultaneous utilization of CO2 and CH4 through dry reforming of methane with Ni–Ce@SiO2 catalyst: Parametric and simulation studies

Intan Clarissa Sophiana, Bambang Heru Susanto, Riezqa Andika, Soen Steven et al.
2 citations
Case Studies in Chemical and Environmental Engineering
Catalysts for Methane Reforming
0.21
article

Simultaneous utilization of CO2 and CH4 through dry reforming of methane with Ni–Ce@SiO2 catalyst: Parametric and simulation studies

Intan Clarissa Sophiana, Bambang Heru Susanto, Riezqa Andika, Soen Steven, Archita Permatasari, Norikazu Nishiyama, Arnetta Revieri
article en
2 citations

Abstract

The dry reforming of methane (DRM) can reduce CO 2 and CH 4 simultaneously. This study utilized East Natuna gas fields, composed of 70 % CO 2 and 30 % CH 4 , for syngas production via DRM using a Ni–Ce@SiO 2 catalyst. The kinetic parameters employed the Langmuir-Hinshelwood mechanism on the surface reaction as the rate-determining step. The simulation results provided an error margin below 5 %. A CO 2 :CH 4 feed ratio of 70:30 at 700 o C achieves higher CH 4 conversion than a 50:50 ratio (97.10 % vs. 79.01 %), yet with lower H 2 /CO ratio (0.68 vs. 0.92). Also, higher temperatures impact shorter reactor lengths and swifter times to reach stable conversion.

Case Studies in Chemical and Environmental EngineeringVol. 11
Bandung Institute of Technology (ID), University of Indonesia (ID), National Nuclear Energy Agency of Indonesia (ID), National Research and Innovation Agency (ID), The University of Osaka (JP)
Universitas Indonesia
Openalex Percentile: Top 58%
Catalysts for Methane Reforming
0.21
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