Abstract
A sequence of unit processes consisting of a berl-saddle-packed-bed anaerobic reactor and an expanded-bed, granular activated carbon fluidized-bed anaerobic reactor was used for the treatment of a synthetically prepared coal conversion wastewater. The wastewater, with high concentrations of inhibitory compounds, was fed at three different chemical oxygen demand (COD) concentrations: 1513, 3027, and 7567 mg/L. Excellent removal of organic matter combined with high conversion of COD to methane was achieved. Negligible removal of COD was observed in the packed-bed reactor whereas the expanded-bed GAC reactor removed the majority of the organics in the wastewater. Ortho- and meta-cresol resisted biodegradation and their toxicity to the anaerobic culture in the GAC reactor was overcome by partial replacement of the granular activated carbon medium in that reactor.
Original language | English (US) |
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Pages (from-to) | 86-92 |
Number of pages | 7 |
Journal | Journal of the Water Pollution Control Federation |
Volume | 60 |
Issue number | 1 |
State | Published - Jan 1 1988 |
Externally published | Yes |
ASJC Scopus subject areas
- Pollution