Experimental Validation of Stationary and Transient Models of a Methanol Demonstration Plant
The system integration of cross‐industrial networks in the Carbon2Chem® project relies on numerical simulations. Hence, this study validates the methanol synthesis loop models vs. the measurements from a demonstration plant, focusing on the thermodynamic, kinetic, and dynamic aspects. The plant can...
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Veröffentlicht in: | Chemie ingenieur technik 2024-09, Vol.96 (9), p.1268-1280 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | The system integration of cross‐industrial networks in the Carbon2Chem® project relies on numerical simulations. Hence, this study validates the methanol synthesis loop models vs. the measurements from a demonstration plant, focusing on the thermodynamic, kinetic, and dynamic aspects. The plant can produce up to 500 L per week of methanol from real blast furnace gases of the thyssenkrupp steel plant in Duisburg. Despite its small size, it comprises a recycle gas loop and an original reactor tube of 6 m in length. After validation, the simulation models are used to analyze the dynamic operation limits of the plant, and they are transferred to the model of an industrial size to analyze the operation of cross‐industrial networks with volatile boundary conditions.
Methanol synthesis loop models are validated via comparison with measurements from a Carbon2Chem® demonstration plant at the C2C Technical Center. The validated models are applied to analyze dynamic characteristics and transferred to models of a planned methanol plant in industrial size, exploring cross‐industrial network operations under volatile conditions. |
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ISSN: | 0009-286X 1522-2640 |
DOI: | 10.1002/cite.202400014 |