Abstract
The creation of anoxic granulated biomass has been monitored in a laboratory USB (Upflow Sludge Blanket) reactor with the volume of 3.6 L. The objective of this research was to verify the possibilities of post-denitrification of residual NO3-N concentrations in treated wastewater (denitrification of 10-20 mg L−1 NO3-N) and to determine the maximum hydraulic and mass loading of the granulated biomass reactor. G-phase from biodiesel production and methanol were both tested as external organic denitrification substrates. The ratio of the organic substrate COD to NO3-N was 6. Only methanol was proven as a suitable organic substrate for this kind of reactor. However, the biomass adaptation to the substrate took over a week. The cultivation of anoxic granulated biomass was reached at hydraulic loading of over 0.35 m h−1. The size of granules was smaller when compared with results found and described in literary reports (granules up to 1 mm); however, settling properties were excellent and denitrification was deemed suitable for the USB reactor. Sludge volume indexes of granules ranged from 35-50 mL g−1 and settling rates reached 11 m h−1. Maximum hydraulic and mass loadings in the USB reactor were 0.95 m3 m−2 h−1 and 6.6 kg m−3 d−1. At higher loading levels, a wash-out of the biomass occurred.
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© 2008 Institute of Chemistry, Slovak Academy of Sciences
Articles in the same Issue
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- Granulation of activated sludge in a laboratory upflow sludge blanket reactor
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- A simple and efficient synthesis of 3-substituted derivatives of pentane-2,4-dione
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- Pyrolytic and catalytic conversion of rape oil into aromatic and aliphatic fractions in a fixed bed reactor on Al2O3 and Al2O3/B2O3 catalysts
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Articles in the same Issue
- Biosynthesis of methanol from methane by Methylosinus trichosporium OB3b
- Influence of reaction medium composition on enzymatic synthesis of galactooligosaccharides and lactulose from lactose concentrates prepared from whey permeate
- Immobilization of modified penicillin G acylase on Sepabeads carriers
- Granulation of activated sludge in a laboratory upflow sludge blanket reactor
- Investigation of the effect of fluid elasticity on a cake filtration process
- Lab-scale testing of a low-loaded activated sludge process with membrane filtration
- Calcium sulphate scaling in membrane distillation process
- Characterization and filtration performance of coating-modified polymeric membranes used in membrane bioreactors
- Informational analysis of the grinding process of granular material using a multi-ribbon blender
- Effects of vessel baffling on the drawdown of floating solids
- N2O catalytic decomposition — effect of pelleting pressure on activity of Co-Mn-Al mixed oxide catalysts
- Intelligent control of a pH process
- Influence of suspended solid particles on gas-liquid mass transfer coefficient in a system stirred by double impellers
- A three-phase nonequilibrium model for catalytic distillation
- Membrane processes used for separation of effluents from wire productions
- A simple and efficient synthesis of 3-substituted derivatives of pentane-2,4-dione
- Formation of hydrated titanium dioxide from seeded titanyl sulphate solution
- Pyrolytic and catalytic conversion of rape oil into aromatic and aliphatic fractions in a fixed bed reactor on Al2O3 and Al2O3/B2O3 catalysts
- Oxidation of thiophene over copper-manganese mixed oxides
- Study of partitioning and dynamics of metals in contaminated soil using modified four-step BCR sequential extraction procedure
- Preparation and properties of a new composite photocatalyst based on nanosized titanium dioxide