Comparison of technology, costs and
environmental benefit of wastewater treatment plants in mountainous areas in the alps
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Karlsbad Refuge

Site description and boundary conditions
Design and treatment efficiency

Site description and boundary conditions

 
boundary conditions

maximum daily organic load [PE]
104
maximum hydraulic load [m3/d]
6
annual organic load [kg BOD/a]
380
altitude [m a.s.l.]
2260
sensitivity [hydrogeology, protected area ...] limestore
lagal requirements [BOD elimination]
80%
operation period [season]
summer
energy supply [type, kW]
aggregate
means of transport [type]
lorry
existing WWTP [type, condition, volume l/PE]
3-chambers, poor condition, 432
 
 
Abb. 4.23
Fig. 4.23: The 3 tanks (prefabricated concrete parts) of the new WWTP at the backside of the Karlsbad Refuge (with Life-monitoring team and refugist)

 
Abb424.jpg
Fig. 4.24: Doubble compressor unit and programmable control unit with magnetic valves in order to control the air flow.

 
 
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Fig. 4.25:   Flow-scheme of the WWTP Karlsbad Refuge



Design and treatment efficiency

Loading of the biological treatment

WWTP Karlsbad Refuge
seasonal average
max. week 
max. day
loading [PE40]
50
80
104
BOD 5-load [kg/d]
2.0
3.2
4.2
influent flow [m3/d]
3.5
5.5
7.0

 

Design according to the F/M ratio in the max. week

V =  12.3 m3 (volume B-tank)

Maerob = 12.3 m 3 x 4 kg SS/m3 x 0.4 = 20 kg SS (aerobic sludge mass)

BSS = 3.2 kg BOD 5 /d / 20 kg TS = 0.16 kg/kg.d (aerobic sludge load)

OB = 3.2 x 2 kg O2 /kg BSB5 / (24 h x 0.4) = 0.67 kg O2/h (oxygen demand)
Compare chapter "oxygen demand"

 

Energy demand

max. power [W]
max. electric work
[kWh/d]
mean electric work
[kWh/d]
1 125
10
7.2


Treatment efficiency

date
[dd.mm.yyyy]
CODeffluent [mg/l] 
NH4-Neffluent [mg/l] 
NO3-Neffluent [mg/l]
CSBelimination [%]
Nelimination [%]
loading
[% of PWmax ]
06.10.2000
585
115
1.0
74
42
 
23.07.2001
120
7
1.0
92
96
 122


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14. Feb 2003