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Updated: Aug 13, 2025

Synthesis and Testing of Supported Pt-Cu Solid Solution Nanoparticle Catalysts for Propane Dehydrogenation
Published on: July 18, 2017
Performance of homogeneous catalysts viewed in dynamics
Wenjun Yang1, Georgy A Filonenko1, Evgeny A Pidko1
1Inorganic Systems Engineering group, Department of Chemical Engineering, Faculty of Applied Sciences, Delft University of Technology, Van der Maasweg 9, 2629 HZ, Delft, The Netherlands. G.A.Filonenko@tudelft.nl.
Catalyst performance assessment needs more than just reaction yields. Transient behaviors and real-time speciation significantly impact catalytic reactions, requiring a comprehensive set of descriptors for accurate evaluation.
Area of Science:
- Catalysis
- Chemical Kinetics
- Materials Science
Background:
- Current catalyst screening often relies solely on reaction yields, overlooking complex system dynamics.
- This simplified approach fails to account for intrinsic catalyst reactivities and transient behaviors.
Purpose of the Study:
- To examine the transient behavior of catalysts during activation, deactivation, and turnover.
- To illustrate how catalyst speciation and reaction environments influence kinetics.
- To propose a more comprehensive depiction of catalytic performance beyond reaction yield.
Main Methods:
- Analysis of catalyst behavior in hydrogenation catalysis as a representative example.
- Investigation of real-time catalyst speciation under various reaction conditions.
- Identification and discussion of catalytically relevant descriptors.
Main Results:
- Catalyst performance is a complex, time-dependent metric influenced by multiple factors.
- Transient processes like activation and deactivation critically affect overall kinetics.
- Real-time catalyst speciation is determined by process dynamics and the reaction environment.
Conclusions:
- Reaction yield alone is insufficient for effective catalyst assessment.
- A multi-descriptor approach is necessary for a comprehensive understanding of catalytic performance.
- The findings are applicable to various catalytic transformations beyond hydrogenation.
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For gas-phase reactions, the equilibrium constant may be expressed in terms of either the molar concentrations (Kc) or partial pressures (Kp) of the reactants and products. A relation between these two K values may be simply derived from the ideal gas equation and the definition of molarity. According to the ideal gas equation:
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