| The study of microreactors involves the miniaturisation of entire reactor systems on to structures ranging from several millimetres to several centimetres in length and height. Their large surface area to volume ratio results in efficient heat and mass transfer. As such, they allow better control of processes and quick quenching, which can lead to improved selectivity and conversion. Safety is improved as their flame trap dimensions prevent flame propagation. Also, previously unfeasible reaction routes may be opened up. Because of the way they are put together, there will be shorter lag time between R and D and industrial application. This is because scale-up is unnecessary, Instead, numbering-up of reactors can be used to increase production capacities. The first step in fabricating a microreactor is to appreciate the varied methods available. The most important and applicable methods are: photolithography, wet bulk machining, dry etching, chemical vapour deposition (CVD), LIGA, laser machining, ultraprecision machining, soft lithography and glass microfabrication. Combinations of these techniques will allow the fabrication of most reactors. In addition, since microfluidic systems typically take the form of thin fabricated sheets carrying different unit operations which can be stacked to form a complete reaction system, bonding techniques are also very important. Examples include anodic bonding, fusion bonding, eutectic bonding and adhesive bonding. A T-microreactor was designed for the gas phase partial oxidation of methanol to formaldehyde over a silver catalyst. It consists of a T-channel etched in silicon with the top of the channel sealed by a piece of glass. While simple, it served to demonstrate the main procedures involved in microfabrication: CVD, photolithography, wet and dry etching, and anodic bonding. Since methanol is a liquid at room temperature, the reactor had to incorporate a pre-heating section to vaporise methanol prior to it entering the reaction section. Three reactor designs (channel width 600 mum and depth 300 mum) were made with differing reaction channel lengths (15, 104 and 207 mm). This was done to widen the range of residence times. Catalyst deposition methods used included evaporation, manual placement of silver wires/foils, electrodeposition and an in-situ chemical reaction, all of which proved inadequate due to combinations of poor adhesion, activity and stability. The sealing of the reactor and the development of suitable interfacing with external equipment proved to be major challenges too, mostly due to the high temperature operation of the reactor. The final product was a silicon microreactor fabricated using Deep Reactive Ion Etching or KOH etching, with silver catalyst deposited through sputtering and sealed by a Pyrex plate through anodic bonding. High conversion was achieved using a mixture of 8.0 - 8.6% methanol and balance oxygen, without any helium to quench the reaction. A micro-falling film reactor (mu-FFR) was used to study the gas-liquid hydrogenation of nitrobenzene over a solid palladium catalyst. A robust catalyst had to be developed that was compatible with the reactor system, in terms of incorporation, suitability for continuous use, longevity and reproducibility. Based on the knowledge gained in this project, a general design algorithm was proposed in order to bring some structure to the discipline of microreactor engineering. It represents a summary and guide to the microreactor design route. A key aspect of this route is the use of modelling to aid in designing microreactors. (Abstract shortened by ProQuest.). |
