Abstract
A simplistic and systematic procedure has been developed for the design and upscaling of a multichannel, continuous-flow electrocoagulation reactor of monopolar configuration for the removal of submicron particles from wastewater. Using wastewater generated from the chemical-mechanical planarization process as the target wastewater, a series of laboratory-scale studies were conducted to determine the required operating conditions for the efficient removal of the ultrafine silica particles. These operating criteria included charge loading (≥8 F/m3), current density (ge;5.7 A/m2), hydraulic retention time (ge;60 min), as well as the initial pH (7-10). Furthermore, a steady-state transport equation with second-order reaction kinetics was employed to describe the rate of coagulation as the rate-limiting factor. The actual kinetic constant determined from the laboratory-scale experiments was approximately 1.2 × 10-21 m3/s, which was three orders of magnitude smaller than that calculated based on Brownian coagulation. The model was subsequently validated with a series of experiments using a pilot-scale electrocoagulation reactor geometrically similar to the laboratory-scale reactor with nearly 20 times volumetric scaleup.
Original language | English |
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Pages (from-to) | 1651-1658 |
Number of pages | 8 |
Journal | Journal of Environmental Engineering |
Volume | 132 |
Issue number | 12 |
DOIs | |
State | Published - Dec 2006 |
Keywords
- Channel flow
- Coagulation
- Colloids
- Kinetics
- Laminar flow
- Silica
- Wastewater management
- Water treatment