Optimal conceptual design of processes with heterogeneous catalytic reactors
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2010
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Metapodaci
Prikaz svih podataka o dokumentuApstrakt
This paper presents an optimisation-based method for the screening and conceptual design of processes with heterogeneous catalytic reactors. The method follows a multi-level approach to process synthesis to establish performance targets and identify high-performance designs. At each level, process superstructures are optimised to explore performance limits of the system and to guide the understanding of the relationships between individual design features and process performance. This enables the design engineer to explore trade-offs between performance and structural complexity in a coordinated manner. The method leads to a number of potential design candidates that provide the design engineers with insight into the performance gains that can be expected by increasing design complexity. The method has been developed and implemented for heterogeneously catalysed gas-phase reaction systems and is illustrated with an example in styrene production.
Ključne reči:
Reaction engineering / Process synthesis / Heterogeneous catalysis / Superstructure optimisation / StyreneIzvor:
Chemical Engineering Journal, 2010, 163, 3, 438-449Izdavač:
- Elsevier Science Sa, Lausanne
DOI: 10.1016/j.cej.2010.08.006
ISSN: 1385-8947
WoS: 000283449400034
Scopus: 2-s2.0-77956650244
Institucija/grupa
Tehnološko-metalurški fakultetTY - JOUR AU - Montolio-Rodriguez, Daniel AU - Linke, Patrick AU - Linke, David AU - Stijepović, Mirko PY - 2010 UR - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/1724 AB - This paper presents an optimisation-based method for the screening and conceptual design of processes with heterogeneous catalytic reactors. The method follows a multi-level approach to process synthesis to establish performance targets and identify high-performance designs. At each level, process superstructures are optimised to explore performance limits of the system and to guide the understanding of the relationships between individual design features and process performance. This enables the design engineer to explore trade-offs between performance and structural complexity in a coordinated manner. The method leads to a number of potential design candidates that provide the design engineers with insight into the performance gains that can be expected by increasing design complexity. The method has been developed and implemented for heterogeneously catalysed gas-phase reaction systems and is illustrated with an example in styrene production. PB - Elsevier Science Sa, Lausanne T2 - Chemical Engineering Journal T1 - Optimal conceptual design of processes with heterogeneous catalytic reactors EP - 449 IS - 3 SP - 438 VL - 163 DO - 10.1016/j.cej.2010.08.006 ER -
@article{ author = "Montolio-Rodriguez, Daniel and Linke, Patrick and Linke, David and Stijepović, Mirko", year = "2010", abstract = "This paper presents an optimisation-based method for the screening and conceptual design of processes with heterogeneous catalytic reactors. The method follows a multi-level approach to process synthesis to establish performance targets and identify high-performance designs. At each level, process superstructures are optimised to explore performance limits of the system and to guide the understanding of the relationships between individual design features and process performance. This enables the design engineer to explore trade-offs between performance and structural complexity in a coordinated manner. The method leads to a number of potential design candidates that provide the design engineers with insight into the performance gains that can be expected by increasing design complexity. The method has been developed and implemented for heterogeneously catalysed gas-phase reaction systems and is illustrated with an example in styrene production.", publisher = "Elsevier Science Sa, Lausanne", journal = "Chemical Engineering Journal", title = "Optimal conceptual design of processes with heterogeneous catalytic reactors", pages = "449-438", number = "3", volume = "163", doi = "10.1016/j.cej.2010.08.006" }
Montolio-Rodriguez, D., Linke, P., Linke, D.,& Stijepović, M.. (2010). Optimal conceptual design of processes with heterogeneous catalytic reactors. in Chemical Engineering Journal Elsevier Science Sa, Lausanne., 163(3), 438-449. https://doi.org/10.1016/j.cej.2010.08.006
Montolio-Rodriguez D, Linke P, Linke D, Stijepović M. Optimal conceptual design of processes with heterogeneous catalytic reactors. in Chemical Engineering Journal. 2010;163(3):438-449. doi:10.1016/j.cej.2010.08.006 .
Montolio-Rodriguez, Daniel, Linke, Patrick, Linke, David, Stijepović, Mirko, "Optimal conceptual design of processes with heterogeneous catalytic reactors" in Chemical Engineering Journal, 163, no. 3 (2010):438-449, https://doi.org/10.1016/j.cej.2010.08.006 . .