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Michael J. Stutz

Researcher at ETH Zurich

Publications -  8
Citations -  446

Michael J. Stutz is an academic researcher from ETH Zurich. The author has contributed to research in topics: Catalysis & Partial oxidation. The author has an hindex of 6, co-authored 8 publications receiving 432 citations.

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A micro-solid oxide fuel cell system as battery replacement

TL;DR: In this article, the concept and the design of a micro-solid oxide fuel cell system is described and discussed, which consists of the fuel cell PEN element, a gas processing unit, and a thermal system PEN elements of freestanding multi-layer membranes are fabricated on Foturan ® and on Si substrates using thin film deposition and microfabrication techniques.
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Effects of microreactor wall heat conduction on the reforming process of methane

TL;DR: In this article, the effect of wall conduction on the performance of an autothermal tubular methane microreformer was investigated numerically, and it was found that axial wall temperature is strongly dependent on the wall inner surface temperature, hence the heat conduction through the channel wall.
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Optimum washcoat thickness of a monolith reactor for syngas production by partial oxidation of methane

TL;DR: In this article, the authors investigated the thermal and diffusive properties of a washcoat of finite thickness that is modeled as a porous layer composed of a ceramic support containing catalytic active rhodium sites.
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Syngas production from butane using a flame-made Rh/Ce0.5Zr0.5O2 catalyst

TL;DR: In this paper, the capability of flame-made Rh/Ce0.5O2 nanoparticles catalyzing the production of H2 and CO-rich syngas from butanewas investigated for different Rh loadings (0.2 wt% Rh) and two different ceramicfibers (Al2O3/SiO2 and SiO2) as plugging material in a packed bed reactor for a temperature range from 225 to 750 8C.
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Optimization of methane reforming in a microreactor- : effects of catalyst loading and geometry

TL;DR: In this article, the effect of the catalyst surface site density (catalyst amount) and reactor geometry on the reforming process of methane in a wall-coated, single-channel microreactor is investigated numerically.