Samenvatting
A pseudo-homogeneous model, considering the axial and radial heat and mass transfer characteristics of an oxidative coupling of methane (OCM) packed-bed catalytic reactor, was utilized to represent its thermal reaction performance in a wide range of variation of the operating conditions investigated in this research. This is another step towards distinguishing the direct contribution of the catalytic reactions and indirect contribution of the reactor's structural characteristics on the overall OCM reactor performance, as well as towards developing a thoroughly representative reaction scheme and a well-estimated set of kinetic parameters. The results of an extensive experimentation were also utilized to support this model-based analysis.
| Originele taal-2 | Engels |
|---|---|
| Pagina's (van-tot) | 694-708 |
| Aantal pagina's | 15 |
| Tijdschrift | Chemical Engineering & Technology |
| Volume | 45 |
| Nummer van het tijdschrift | 4 |
| DOI's | |
| Status | Gepubliceerd - apr. 2022 |
Bibliografische nota
Publisher Copyright:© 2022 The Authors. Chemical Engineering Technology published by Wiley-VCH GmbH.
Financiering
Financial support from the Cluster of Excellence ?Unifying Concepts in Catalysis? (UniCat, EXC314) funded by the German Research Foundation ? Deutsche Forschungsgemeinschaft is appreciated. Open access funding enabled and organized by Projekt DEAL. The authors have declared no conflict of interest. We acknowledge Dr. Champakali Ayyub for her critical inputs and constant support. TIFR kitchen staff for help with fly media preparation and maintenance. We specially thank the members of UK laboratory, TIFR for useful discussions and constructive comments. This research has been supported by funds to U.K.‐S. {DAE‐TIFR (Government of India grant—12P0122), Department of Biotechnology (DBT, India grant BT/PR4972/AGR/36/714/2012) and Swarnajayanti fellowship (DST Government of India grant DST/SJF/LSA‐02/2012‐13)}.
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