Case study - Veolia Water Solutions & Technologies
Case study - Veolia Water Solutions & Technologies
Case study - Veolia Water Solutions & Technologies
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<strong>Case</strong> <strong>study</strong><br />
GARDERMOEN TREATMENT PLANT<br />
- OSLO, NORWAY<br />
Challenge<br />
In June 1996 AnoxKaldnes was contracted to build a<br />
wastewater treatment system for the municipality of<br />
Ullensaker. It was decided by the Norwegian pollution<br />
control authorities that a new system be built because<br />
the old plant was not able to handle the special<br />
demands of a new airport.<br />
Located in close proximity to the Oslo International<br />
Airport, the new Gardermoen Wastewater Treatment<br />
plant faced many challenges. Firstly, it had to be covered<br />
in part because it is a tradition in Norway to provide<br />
a good working environment for the operators<br />
i.e. eliminating annoying odours, noise and aerosols<br />
and also because open basins would attract birds and<br />
create a hazard for the airplanes.<br />
Highlights<br />
General information<br />
Gardermoen Treatment Plant - Oslo, Norway<br />
The Gardermoen treatment plant was constructed<br />
to treat wastewater from the new Oslo International<br />
Airport as well as the surrounding communities of<br />
Ullensaker and Nannestad.<br />
Concept<br />
Spent aircraft de-icing fluid is a major pollution concern<br />
at airports especially in areas with severe winter<br />
climates. Currently Monopropylene Glycol (MPG) is<br />
used for de-icing and during the planning process,<br />
tests showed that it would be feasible to use runoff<br />
from airport de-icing platforms as an external carbon<br />
source for denitrification at the new plant.<br />
OPERATIONAL SINCE: October 1998<br />
Challenge<br />
To treat complex airport wastewater combined with<br />
de-icing fluid and municipal wastewater from nearby<br />
communities.<br />
Solution<br />
Utilize the Kaldnes MBBR biofilm process for biological<br />
Nitrogen removal, preceded by<br />
primary treatment and followed by chemical precipitation<br />
of Phosphorous and DAF for particle separation.<br />
Effluent requirements<br />
Total Phosphorous: 95% Removal (annual average)<br />
- Average Concentration 0.25 mg/L<br />
Total Nitrogen:<br />
BOD 7<br />
:<br />
- Max. Concentration 0.5 mg/L<br />
70% Removal (annual average)<br />
70% Removal (annual average)<br />
- Average Concentration 10 mg/L<br />
- Max. Concentration 20mg/L
Design<br />
The plant is constructed and designed for pre- and<br />
post-denitrification. The external carbon source, the<br />
MPG from the airport, is hence used for post-denitrification.<br />
The biological treatment is followed by flocculation<br />
and flotation for separation of sludge.<br />
DESIGN LOAD<br />
Dimensioning Flow: 920 m/h<br />
Maximum Flow: 1,300 m/h<br />
TBOD7 : 2,680 kg/d<br />
TCOD: 5,480 kg/d<br />
SS: 3,290 kg/d<br />
TN: 704 kg/d<br />
TP: 101 kg/d<br />
Temperature Range: 4 o C - 14 o C<br />
Results<br />
Excellent plant performance since start-up.<br />
Total nitrogen removal efficiency in 2001 was more<br />
than 80% annual average.<br />
y<br />
c<br />
c<br />
Performance Year 2000<br />
In Out Removal<br />
BOD 7<br />
210 6.6 97%<br />
COD 559 34 94%<br />
TN 46 3 93%<br />
TP 7.05 0.18 97%<br />
SS 307 9 97%<br />
y<br />
c<br />
c<br />
info@anoxkaldnes.com<br />
www.anoxkaldnes.com<br />
AnoxKaldnes<br />
Klosterängsvägen 11A<br />
SE-226 47 Lund, Sweden<br />
Tel. +46 46-18 22 00<br />
Fax. +46 46-13 32 01