TY - JOUR
T1 - Consequence of products from oxidative coupling of methane in a non-oxidative high temperature environment
AU - Komada, Haruka
AU - Obata, Keisuke
AU - Li, Duanxing
AU - Sarathy, Mani
AU - Takanabe, Kazuhiro
N1 - KAUST Repository Item: Exported on 2023-03-22
Acknowledgements: This work was supported by MHI Innovation Accelerator LLC.
PY - 2023/2/2
Y1 - 2023/2/2
N2 - Oxidative coupling of methane (OCM) is a direct process that converts methane to higher hydrocarbons, such as ethylene. For several decades, various catalysts and their reaction mechanisms have been investigated to obtain high selectivity for the target products. However, the consequences of OCM products after O2 depletion at high temperatures, which is generated by an exothermic reaction, have been often overlooked. In the present study, a two-stage reactor that mimics an industrial reactor was used to study the successive reactions of OCM products. Gas phase homogeneous and heterogeneous reactions on the surface of catalysts and supports have been systematically investigated. Dehydrogenation of OCM products to acetylene and the following condensation occurs in the gas phase. Meanwhile, steam reforming of OCM products concurrently followed by water gas shift reactions was observed on various catalysts and supports and led to the loss of C2 yield. Based on the investigations, a design guideline for the OCM reactor is proposed.
AB - Oxidative coupling of methane (OCM) is a direct process that converts methane to higher hydrocarbons, such as ethylene. For several decades, various catalysts and their reaction mechanisms have been investigated to obtain high selectivity for the target products. However, the consequences of OCM products after O2 depletion at high temperatures, which is generated by an exothermic reaction, have been often overlooked. In the present study, a two-stage reactor that mimics an industrial reactor was used to study the successive reactions of OCM products. Gas phase homogeneous and heterogeneous reactions on the surface of catalysts and supports have been systematically investigated. Dehydrogenation of OCM products to acetylene and the following condensation occurs in the gas phase. Meanwhile, steam reforming of OCM products concurrently followed by water gas shift reactions was observed on various catalysts and supports and led to the loss of C2 yield. Based on the investigations, a design guideline for the OCM reactor is proposed.
UR - http://hdl.handle.net/10754/690509
UR - http://xlink.rsc.org/?DOI=D2CY02145E
UR - http://www.scopus.com/inward/record.url?scp=85149967045&partnerID=8YFLogxK
U2 - 10.1039/d2cy02145e
DO - 10.1039/d2cy02145e
M3 - Article
SN - 2044-4753
JO - Catalysis Science and Technology
JF - Catalysis Science and Technology
ER -