Abstract

The present electrode configuration and arrangement of the electrostatic precipitator (ESP) have been determined, based on experimental data from the laboratory scale ESP and operational experiences of the full-scale ESPs. However, there is a limitation to determine the optimal electrode design. As an alternate approach, the numerical simulation was investigated. A two-dimensional electrohydrodynamic (EHD) simulation for the wire electrode in the duct geometry was first carried out. Then, the experimental study and operational results of a full-scale ESP on the voltage–current characteristics were investigated. An applicable simulation model of electrical characteristics for the full-scale ESP was developed. Next, three-dimensional EHD simulation was carried out in order to understand the flow distribution for the typical industrial ESP geometry i.e. the spiked-type discharge electrode and convex–concave-type collecting electrode, in which the primary flow becomes three-dimensional due to ionic wind. The three-dimensional EHD simulation shows that the flow interaction due to ionic wind takes place at every spiked electrode region and a zig–zag motion is formed in the direction of the primary flow. The magnitude of the flow interaction is described by using dimensionless EHD number ( N EHD). The flow interaction in the typical ESP is not significantly large because the N EHD of the full-scale ESP is usually less than 1.0.

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