Abstract

Open-cell foams are promising catalyst supports as they provide a low pressure drop, radial mixing, and exceptional heat transport properties. Even though their large potential for the design of small-scale, dynamically operated reactors with strongly exothermic reactions is known, their application is not yet common. To design efficient and safe structured reactors in the future, the understanding of structure-heat transport relations is key. Fully resolved CFD simulations of non-isothermal structured reactors including chemical surface reactions require a high modeling effort and are computationally expensive. In a previous study we therefore implemented volumetrically distributed heat sources in the solid to mimic the heat production during an exothermal reaction, and evaluated the resulting heat flows and temperature distributions via CFD. The previous analysis, however, was limited to one specific open-cell foam geometry. In this study, we extend the conjugate heat transfer problem including heat production in the solid to five periodic open-cell foams (Kelvin cell-lattices) with defined but different structural parameters to establish structure-heat transport relations. We confirmed conduction being the dominant heat removal mechanism and found the strut diameter and the solid thermal conductivity being the key parameters to improve heat transport and reduce hot spots.

Highlights

  • Cellular and interconnected open-cell foam structures provide a remarkable potential for process intensification in, among others, solar receivers, pore burners, and catalytic reactors (Wu and Wang, 2013; Gao et al, 2014; Kiewidt and Thöming, 2019a)

  • Cell lattices have geometric properties that are relevant in heterogeneous catalysis and are suitable for the investigation of heat production in different foam geometries

  • The high influence of the strut diameter and the thermal conductivity underpins the impact of thermal conduction in the solid domain

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Summary

Introduction

Cellular and interconnected open-cell foam structures provide a remarkable potential for process intensification in, among others, solar receivers, pore burners, and catalytic reactors (Wu and Wang, 2013; Gao et al, 2014; Kiewidt and Thöming, 2019a). Their potential for intensification of exo- and endothermic catalytic reactions is based on their outstanding radial heat transport, high radial mixing, and low pressure loss (Bianchi et al, 2012; Gräf et al, 2014). For small-scale dynamic reactors, which are needed in the future for Power-to-X (PtX) processes, open-cell foams provide resilient heat transport over

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