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

Site description and boundary conditions
Design and treatment efficiency

Site description and boundary conditions


boundary conditions

maximum daily organic load [PE]
110
maximum hydraulic load [m3/d]
11
annual organic load [kg BOD/a]
230
altitude [m a.s.l.]
1708
sensitivity [hydrogeology, protected area ...] granite, creek
legal requirements [BOD elimination]
80%
operation period [season]
summer
energy supply [type, kW]
water power plant, 22
means of transport [type]
lorry
existing WWTP [type, condition, volume l/PE]
8-chambers, good condition, 190
 
 
Abb. 4.26
Fig. 4.26: View of the WWTP Konstanz Refuge showing the 3 septic tanks at the left hand side and the tanks of the Biocos- System at the right hand side.

 
 
Abb. 4.27
Fig. 4.27:   Flow-scheme of the WWTP Konstanz-Refuge.

 
Abb. 4.28
Fig. 4.28: Reuse of all existing tanks with new applications required a new piping of the wastewater-, air- and control-lines.

 

Design and treatment efficiency

Loading of the biological treatment

WWTP Konstanz Refuge
seasonal average
max. week 
max. day
loading [PE40]
38
85
110
BOD5-load [kg/d]
1.5
3.4
4.4
influent flow Q [m3/d]
4.2
8.0
11.0

 

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

Vaerob =  7.2 m3 (volume B-tank)

Maerob = 7.2 m 3 x 4 kg SS/m3  = 28.8 kg SS (aerobic sludge mass)

BSS = 3.4 kg BOD5/d / 28.8 kg SS = 0.12 kg/kg.d (aerobic sludge loading)

OB = 3.4 x 3 kg O2 /kg BOD5 / 24 h = 0.42 kg O2/h (oxygen demand)

 

Energy demand

max. power [W]
max. electric work
[kWh/d]
mean electric work
[kWh/d]
475
11.2
11.2


Treatment efficiency

date
[dd.mm.yyyy]
CODeffluent [mg/l] 
NH4-Neffluent [mg/l] 
NO3-Neffluent [mg/l]
CODelimination [%]
Nelimination [%]
loading
[% of PEmax ]
12.08.1999
30
13
14
97
77
 
25.09.2000
40
0
19
97
77
 67
17.07.2001
24
12
35
98
65
28


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28. Mar 2002