Titlebook: Microreaction Technology; IMRET 5: Proceedings Michael Matlosz,Wolfgang Ehrfeld,Jörg Peter Baselt Conference proceedings 2001 Springer-Verl

interference

不能和解

Design, Fabrication And Experimental Study Of New Compact Mini Heat-Exchangersrial, and the method of fabrication. The overall dimensions are of the order of several centimetres, while the internal channels have characteristic dimension in the millimetre range. The different “layers” or plates and their channels may be designed in such way as to produce an important local mix

投射

Development of a Self-Heating Catalytic Microreactor The channel (upper width = 600 μm, lower width = 515 μm, depth = 60 μm, and length = 78 mm) on one side was used as a reactor. A heating element (Pt wire) was installed in the channel on the opposite surface of the reactor channel, and a thermocouple was installed in a channel adjacent to the react

geriatrician

Generosity

激怒某人

Design and Fabrication of Zeolite-containing Microstructuresnductor technology was employed in the fabrication of micromachined silicon structures. MFI-type zeolites were grown in-situ on silicon supports by hydrothermal synthesis. Another new fabrication procedure was developed based on microelectronic fabrication and zeolite thin film technologies. The fab

乳白光

光滑

Macroscale production of microsystems of micromachining techniques has largely been developed from the semiconductor industry. For example etching techniques such as electron beam etching, wet chemical etching, focused ion beam machining and constructive techniques such as LIGA.

无意

Prediction of the potential of microreactors for heterogeneously catalysed gas phase reactionsnology to predict the feasibility of applying this technology for a specific synthesis in a microreactor. The program consists of two parts. In the first part basic process equations and parameters and a simplified model of the microreactor are used to obtain preliminary information on the applicabi

傻

Microchannel reactors for kinetic measurement: Influence of diffusion and dispersion on experimentalogeneously catalysed reactions. In addition to excellent heat management for accurate temperature control and the ability to work with small volumes of highly reactive or hazardous products, microreactors should also exhibit enhanced mass transfer from the bulk fluid to the catalyst-coated walls due