## Abstract The degradation of high concentrations of phenol (1g/dm^β3^) in aqueous media at high temperatures (100β190 Β°C) and pressures (2.0 MPa) has been studied by catalytic wet air oxidation in a trickleβbed reactor. The effect of reaction temperature, weight hourly space velocity (WHSV) and h
Prevention of clogging in a biological trickle-bed reactor removing toluene from contaminated air
β Scribed by Frans J. Weber; Sybe Hartmans
- Publisher
- John Wiley and Sons
- Year
- 1996
- Tongue
- English
- Weight
- 749 KB
- Volume
- 50
- Category
- Article
- ISSN
- 0006-3592
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β¦ Synopsis
Removal of organic compounds like toluene from waste gases with a trickle-bed reactor can result in clogging of the reactor due to the formation of an excessive amount of biomass. We therefore limited the amount of nutrients available for growth, t o prevent clogging of the reactor. As a consequence of this nutrient limitation a lower removal rate was observed. However, when a fungal culture was used to inoculate the reactor, the toluene removal rate under nutrient limiting conditions was higher. Over a period of 375 days, an average removal rate of 27 g C/ (m3 h) was obtained with the reactor inoculated with the fungal culture. From the carbon balance over the reactor and the nitrogen availability it was concluded that, under these nutrient-limited conditions, large amounts of carbohydrates are probably formed. We also studied the application of a NaOH wash to remove excess biomass, as a method t o prevent clogging. Under these conditions an average toluene removal rate of 35 g C/(m3 ht was obtained. After about 50 days there was no net increase in the biomass content of the reactor. The amount of biomass which was formed in the reactor equaled the amount removed by the NaOH wash.
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