E.R. Delsman

TL;DR: In this article, a three-dimensional computational fluid dynamics (CFD) model was used to calculate the flow distribution on a microstructured plate, and nine different plate geometries were studied at flow rates between 0.1 and 100 m s−1, or 4 × 10−4 to 0.4 m3 h−1 per plate.

TL;DR: In this article, the authors describe the design, model simulation, and experimental validation and operation of a microdevice for the preferential oxidation of carbon monoxide in hydrogen-rich reformate gas.

TL;DR: In this article, the authors describe the design, experimental, and modelling work concerning a microdevice for the preferential oxidation of carbon monoxide in hydrogen-rich reformate gas, which consists of two heat exchangers and one reactor, all integrated in a single stack of microstructured plates.

TL;DR: A review on selective oxidations is presented in this paper, where the authors focus on catalytic gas-phase oxidation reactions in micro-reactors, typically being performed in wall-coated micro-channels.

TL;DR: In this paper, a comparative study is performed between micro-reactor technology and conventional reactor technology for the case of methanol fuel processing for portable power generation, and the results show that the microreactor can compete with or replace current conventional reactors in production processes.