Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
584282 | Journal of Hazardous Materials | 2007 | 7 Pages |
Abstract
Carbon adsorption process is tested for removal of high concentration of organic mercury (thimerosal) from industrial process wastewater, in batch and continuously flow through column systems. The organic mercury concentration in the process wastewater is about 1123Â mg/L due to the thimerosal compound. Four commercially available adsorbents are tested for mercury removal and they are: Calgon F-400 granular activated carbon (GAC), CB II GAC, Mersorb GAC and an ion-exchange resin Amberlite GT73. The adsorption capacity of each adsorbent is described by the Freundlich isotherm model at pH 3.0, 9.5 and 11.0 in batch isotherm experiments. Acidic pH was favorable for thimerosal adsorption onto the GACs. Columns-in-series experiments are conducted with 30-180Â min empty bed contact times (EBCTs). Mercury breakthrough of 30Â mg/L occurred after about 47Â h (96 Bed Volume Fed (BVF)) of operation, and 97Â h (197 BVF) with 120Â min EBCT and 180Â min EBCT, respectively. Most of the mercury removal is attributed to the 1st adsorbent column. Increase in contact time by additional adsorbent columns did not lower the effluent mercury concentration below 30Â mg/L. However, at a lower influent wastewater pH 3, the mercury effluent concentration decreased to less than 7Â mg/L for up to 90Â h of column operation (183 BVF).
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Authors
Magdalena Velicu, Hongxiang Fu, Rominder P.S. Suri, Kevin Woods,