Microreactor

A microreactor or microstructured reactor or microchannel reactor is a device in which chemical reactions take place in a confinement with typical lateral dimensions below 1 mm; the most typical form of such confinement are microchannels. Microreactors are studied in the field of micro process engineering, together with other devices (such as micro heat exchangers) in which physical processes occur. The microreactor is usually a continuous flow reactor (contrast with/to a batch reactor). Microreactors offer many advantages over conventional scale reactors, including vast improvements in energy efficiency, reaction speed and yield, safety, reliability, scalability, on-site/on-demand production, and a much finer degree of process control. History Gas-phase microreactors have a long history but those involving liquids started to appear in the late 1990s. One of the first microreactors with embedded high performance heat exchangers were made in the early

Microchannel cooling for the LHCb VELO Upgrade I

Victor Coco, Alessandro Mapelli, Giulia Romagnoli

The LHCb VELO Upgrade I, currently being installed for the 2022 start of LHC Run 3, uses silicon microchannel coolers with internally circulating bi-phase CO2 for thermal control of hybrid pixel modules operating in vacuum. This is the largest scale application of this technology to date. Production of the microchannel coolers was completed in July 2019 and the assembly into cooling structures was completed in September 2021. This article describes the R & D path supporting the microchannel production and assembly and the motivation for the design choices, together with the achieved fluidic and thermal performance. The Thermal Figure of Merit of the microchannel coolers is measured on the final modules to be between 1.5 and 3.5 K cm(2) W-1, depending on glue thickness. The microchannel coolers constitute 18% of the total radiation length of the VELO and less than 2% of the material seen before the second measured point on the tracks. Microchannel cooling is well suited to the VELO implementation due to the uniform mass distribution, close thermal expansion match with the module components and resistance to radiation.

ELSEVIER2022

Development of a novel microreactor-based calorimeter for the study of fast exothermal reactions in liquid phase

Marie-Agnès Schneider

Following several tragic chemical accidents that have occurred in recent years, some directives concerning chemical process safety have been issued. The Seveso directive, for example, requires a precise description of the consequences of a possible chemical accident assuming a worst-case scenario. However, to build such scenarios and, hence, make chemical processes safe, profound knowledge of the kinetic and thermal parameters of the reactions in question is necessary. These parameters are usually determined by calorimetric methods. However, in the existing commercial calorimeters the characterization of fast, exothermal reactions raises several problems. Indeed, on the one hand, it is difficult to maintain the isothermal conditions required to determine the kinetics simply and precisely. On the other hand, the calorimeter should be able to measure the heat flow generated as soon as the reactants are brought into contact. It should be able to do this without the need for a period of thermal equilibration that would perturb the measurements, and without any limitations due to the mixing of the reactants. The aim of this work is to develop a calorimetric method that is particularly adapted to studying fast exothermal reactions. The proposed system combines a microreactor with a commercially available microcalorimeter. In the first part of this project a flexible technique for constructing microreactors was chosen. The technique had to be precise, reproducible and inexpensive. The geometry of the microreactor had to fit into the cavity of the commercially available microcalorimeter. The technique chosen was the silk-screen printing of a thick film dielectric. This method makes it possible to build quickly and at low cost numerous microreactors that can be regarded as disposables. The geometry of the reaction channel can be varied and can be adapted to the type of reaction. Once the microreactors were built, the degree of mixing obtained in the microchannels was estimated first by simulation and then by experiment. The flow in the reaction channel was found to be purely laminar and the mixing time corresponded to the time for radial diffusion. Due to the small size of the channels, the mixing time was found to be adequate and not limiting for the characterization of fast reactions. The microreactor was then inserted into the cavity of the commercial calorimeter. The resulting microsystem was calibrated using the neutralization reaction of sulphuric acid with NaOH. This system was further modified to optimize the thermal transfer between the reaction channel and the sensor of the microcalorimeter and to increase its thermal efficiency. Finally, an electrical preheating system of the incoming liquids was put in place and tested. Once the quality of the thermal signal had been optimized, kinetic studies of chemical reactions could be undertaken. First, a model reaction was studied in order to validate the results obtained with the microsystem and to avoid the risk of systematic errors. In the second stage, a previously unknown fast exothermal reaction was characterized. The heat flows measured during the reaction reached 160'000 W·kg-1 but the conditions, however, remained completely isothermal. The global kinetics of this reaction as well as its activation energy were determined.

EPFL2004

Development of a novel microreactor-based calorimeter for the study of fast exothermal reactions in liquid phase

Marie-Agnès Schneider

EPFL2004

Microchannel cooling for the LHCb VELO Upgrade I

Development of a novel microreactor-based calorimeter for the study of fast exothermal reactions in liquid phase

Microchannel reactors for partial oxidation of isopropene

Microchannel cooling for the LHCb VELO Upgrade I

Microchannel reactors for partial oxidation of isopropene

Development of a novel microreactor-based calorimeter for the study of fast exothermal reactions in liquid phase