Abstract
Biogas, generated from an expanded granular sludge bed (EGSB) reactor treating municipal solid waste (MSW) leachate, was recirculated for calcium removal from the leachate via a carbonation process with simultaneous biogas purification. Batch trials were performed to optimize the solution pH and imported biogas (CO2) for CaCO3 precipitation. With applicable pH of 10-11 obtained, continuous trials achieved final calcium concentrations of 181-375mg/L (removal efficiencies≈92.8-96.5%) in the leachate and methane contents of 87.1-91.4% (purification efficiencies≈65.4-82.2%) in the biogas. Calcium-balance study indicates that 23-986mgCa/d was released from the bio-system under the carbonized condition where CaCO3 precipitating was moved outside the bioreactor, whereas 7918-9517mgCa/d was trapped into the system for the controlled one. These findings demonstrate that carbonation removal of calcium by biogas recirculation could be a promising alternative to pretreat calcium-rich MSW leachate and synergistically to improve methane content.
| Original language | English |
|---|---|
| Pages (from-to) | 317-323 |
| Number of pages | 7 |
| Journal | Bioresource Technology |
| Volume | 173 |
| DOIs | |
| State | Published - 1 Dec 2014 |
| Externally published | Yes |
Keywords
- Biogas purification
- Biogas recirculation
- Calcium removal
- EGSB
- MSW leachate