Multi-substrate analysis of carbon oxidation and nitrification in an upflow packed-bed biofilm reactor
✍ Scribed by Shafkat A. Beg; Mirza M. Hassan; Muhammad A. S. Chaudhary
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 1995
- Tongue
- English
- Weight
- 873 KB
- Volume
- 64
- Category
- Article
- ISSN
- 0268-2575
No coin nor oath required. For personal study only.
✦ Synopsis
The performance of an upflow packed-bed biofilm reactor (UPBR) was analysed under multi-substrate limitation by considering simultaneous carbon oxidation and nitrification reactions. Numerical solutions of the proposed model defining the system were obtained for a wide range of operating conditions to illustrate individual substrate limitation behaviour. For an inlet concentration of 75 mg dm-3 of NHi-N and 25 mg dm-3 of methanol, the organic substrate was consumed rapidly near the inlet of the reactor while most of the NHf-N was converted in the central region. The concentration profiles within the biofilm indicated that oxygen was limiting near the inlet of the reactor while organic substrate was limiting at the middle of the reactor. Both NHf-N and methanol became limiting near the reactor exit. Detailed analyses were carried out for a wide range of NHf-N concentrations and for a given concentration of methanol which showed that oxygen could also become limiting even at the middle of the reactor.
📜 SIMILAR VOLUMES
The performance of an upÑow packed-bed bioÐlm reactor was investigated by considering simultaneous methanogenesis and denitriÐcation reactions under step and sinusoidal variations of feed concentration and temperature. For simultaneous step inputs of 20 mg dm~3 of and 60 mg dm~3 of meth-NO 3 ~wN ano
## Abstract **BACKGROUND:** The modelling of simultaneous denitrification and methanogenesis (DM) in upflow packed‐bed biofilm reactors (UPBR) and the effect of inhibition by nitrogen compounds on methanogenesis has received little attention. This study evaluated the effect using a model that incor