A micro plasma reactor for fluorinated waste gas treatment

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Abstract

A microreactor based on a micro-structured electrode (MSE) system is presented. With radio frequency electric power applied to the interdigitated, comb-like capacitor structure a homogeneous plasma is driven at atmospheric pressure with low ignition voltages due to small electrode gaps. The MSE is micromachined by plating nickel onto alumina ceramics. A micromachined Foturan® structure with inlet and outlet channels for the gas flow serves as a reaction chamber. The design of the reactor cell is arranged in a 4×4-array in a multireactor system. The performance of the reactor is modeled with computational fluid dynamics (CFD), used to improve the reactor design. Experiments show that CF4 decomposition rates of over 70% can be achieved at atmospheric pressure.

Introduction

Up to now microreactors were mainly used because of their supreme surface to volume ratio in order to increase heat exchange and exposition effect of catalysts to media. The micro plasma reactor described in this paper makes use of very small electrode gaps between micro-structured electrodes (MSE) with an interdigitated arrangement as shown in Fig. 1 as (1). Advantages are low ignition voltages and an essentially homogeneous plasma at high pressure. The small gaps and planar geometry of the structure require micromachining via photolithography. The MSE are radio frequency (RF) driven and allow to generate large-area uniform glow discharges in He and Ne at pressures above 1500 mbar and in Ar and N2 up to 1200 mbar. The discharges are non-thermal [1] and up to 500 mbar the plasma covers the whole electrode system. By breaking up bonds with high-energy electrons non-thermal plasma allows processing of reactions, which need more than 1000 °C in conventional thermal systems. Thus, a higher energy efficiency is given. One application which is investigated in this work is the decomposition of fluorinated waste gas as produced by semiconductor industry [2], [3].

Section snippets

Design and micromachining of the reactor

Although MSE systems by itself can be used to drive chemical reactions [4], this reactor enhances effectiveness by thorough control of the gas flow. Due to the incorporation of fluorine chemistry the number of applicable materials is limited. Alumina substrates, electroplated nickel and Foturan® with an alumina coating were used as construction materials.

The MSE is plated 100 μm thick from a nickel bath of the sulphamate type [5]. Limited throwing power is partially compensated by current thiefs

Simulation

Simulation of the reactive gas flow in a single cell is performed with computational fluid dynamics (CFD) with the commercial package CFDRC-ACE+ from CFDRC Corporation, Huntsville. A 2D-model is used in order to limit computation time. The flow resistance of the lamellae at the front and end of the chamber is modeled by a narrow slit. The model predicts that a pressure difference of 40 Pa results in a gas flow of 50 sccm. The gas mixture for chemical reactions contains He with 5% CF4, 5% H2 and

Experimental: decomposition of CF4

Both the microreactor and the multireactor are installed onto a complex gas flow and water-cooling system inside a vacuum chamber. The entire experimental setup is described in detail elsewhere [1], [4], [9], [10]. A gas flow rate between 1 and 200 sccm is set up by means of mass flow controllers. For online detection of the plasma product gases a differentially pumped quadrupole mass spectrometer (Pfeiffer Vacuum QMS 200) is used. The discharges are generated using an RF power supply at 13.56 

Conclusions

It is shown that MSE based microreactors can be used for processing in harsh environments including fluorine chemistry, high pressure and high electron energies. Effective flow control can be applied by microstructures and shows great effect on decomposition efficiency. These properties give it capability to handle the abatement of fluorinated waste gas of semiconductor industry with high energy efficiency.

For the handling of large exhaust gas flows it is necessary to perform a numbering-up

Acknowledgements

This work was supported by the Bundesministerium für Bildung und Forschung (bmb + f), Germany, under contract No. 03D0070B/6. We also wish to thank our project partners Dr. T.R. Dietrich and A. Freitag of mgt mikroglas technik AG, Mainz and Dr. L. Fabian of centrotherm Elektrische Anlagen GmbH & Co. KG, Dresden.

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