Anaerobic filter treatment of fishery wastewater
β Scribed by P. Prasertsan; S. Jung; K. A. Buckle
- Publisher
- Springer
- Year
- 1994
- Tongue
- English
- Weight
- 188 KB
- Volume
- 10
- Category
- Article
- ISSN
- 1573-0972
No coin nor oath required. For personal study only.
β¦ Synopsis
Anaerobic treatment of wastewater from a selected seafood processing plant was conducted at organic loading rates (OLR) ranging from 0.3 to 1.8 kg chemical oxygen demand (COD)/m3.day and hydraulic retention times (HRT) ranging from 36 to 6 days. COD reduction decreased with increasing OLR. More than 75% COD reduction could be maintained up to an OLR of about I kg COD/m3.day with an HRT of 11 days. An OLR of 1.3 kg COD/m3.day corresponding to an HRT of 6.6 days gave maximal biogas productivity of 1.5 m3/m3.day or 1.3 m 3 biogas/kg COD with a 65% COD reduction. If the HRT was kept constant at 11 days, an OLR of 1.3 kg COD/m3.day achieved maximal biogas productivity (1.1 m3/m3.day) and yield (0.75 m3/kg COD) and a 60% COD reduction for treatment of tuna condensate.
π SIMILAR VOLUMES
The by-products, molasses, of the sugar industry are used as a source of biomass. Torula yeast is obtained from molasses fermentation and used as animal food. After the separation of the yeast, a highly concentrated wastewater is produced. At present, the wastewater is spread on the land or dischar
A process train consisting of the following sequence of unit processes, a berl-saddle-packed anaerobic filter, an expanded bed, granular activated carbon anaerobic filter, and an activated sludge nitrification system was evaluated for the treatment of a synthetically prepared coal gasification waste