Abstract
This study evaluated the system performance in terms of sorbent usage rate (SUR) of single column, two-column parallel, and lead-lag configurations, both with and without bypass blending, based on two normalized parameters describing the breakthrough profile (mass transfer zone length to lag ratio, or MTZ:Lag) and treatment objective (C/Co). The pore surface diffusion model was used to simulate a range of single compound scenarios to develop a framework for comparing configurations. From this analysis, regions on a MTZ:Lag versus C/Co plot could be identified in which particular configurations yielded the lowest system SUR. At low MTZ:Lag ratios, bypass blending (single column or lead-lag operation) offered significant improvements because of the ability to bypass untreated flow and reduce sorbent bed mass. However, at low target C/Co values, bypass offered little improvement. Lead-lag without bypass performed best at high MTZ:Lag ratios by passing the mass transfer zone through two columns in series. At high MTZ:Lag ratios and high target C/Co values, two-column parallel configurations yielded significant benefits by blending high and low concentration effluents and improving sorbent utilization.
Original language | English (US) |
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Pages (from-to) | 554-563 |
Number of pages | 10 |
Journal | Journal of Environmental Engineering (United States) |
Volume | 139 |
Issue number | 4 |
DOIs | |
State | Published - Apr 1 2013 |
Keywords
- Activated carbon
- Drinking water
- Fixed-bed models
- Sorption
- Water treatment
ASJC Scopus subject areas
- Environmental Engineering
- Environmental Chemistry
- Civil and Structural Engineering
- General Environmental Science