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• Why co-digestion on wastewater
treatment plants?
• Recycling of used coffee capsules
• Management of contraries (metal,
glass, sand) in AD
• Open questions, outlook
Overview
Principle of co-digestion on WWTP
Co-substrates
primary sludge
biogas
dewatered sludge
excess sludge
rejection water
Co-digestion of biowaste on WWTP
• ~ 10.000 digesters on WWTP in the EU
• Most of them have relevant capacities for
additional, external substrates
• Existing infrastructure, qualified personnel
• Investment costs for co-digestion low
(storage tank for substrates, pipes and
pumps, ~ 100.000 €).
• Collection and pre-treatment of co-
substrates by external companies
Co-digestion on WWTP
Energy balance on WWTP
• Germany, Austria: average of 43 % self-
production of electrical power from biogas
produced from sewage sludges
• co-digestion: energy self sufficient WWTP
can be realised
• Co-substrates: separatly collected
biowaste, kitchen waste, waste from dairy
industries….
Co-digestion on WWTP
Energy balance of WWTP Zirl, Tyrol, Austria
Co-digestion on WWTP
0
100.000
200.000
300.000
400.000
500.000
600.000
700.000
800.000
900.000
2006 2007 2008 2009 2010 2011 2012 2013 2014
Bio
gas
[Nm
3/a
)
Biogas from sewage sludge Biogas from Co-substrates
0
200
400
600
800
1.000
1.200
1.400
2006 2007 2008 2009 2010 2011 2012 2013 2014
Ele
ctri
city
[kW
h/a
)
Production electricity Consumption electricity • Total consumption of
electricity ~ 1000 kWh/a
• Dosage of co-substrates
started in 2008.
• From 2009 to 2014:
surplus of electricity
• 2014: problems with
digester foaming,
reduction of substrate
dosage
Recycling of used coffee capsules
Co-digestion on WWTP
• Lifestyle products“ in
food industry e.g. coffee
capsules
• Special challenge for
waste recycling
• Used capsules: coffee
powder and a capsule
made of aluminum
• Used coffee powder biogas production
• Aluminum metal recycling
• Collection and pretreatment of the used
capsules required
Recycling of used coffee capsules
Co-digestion on WWTP
• Separate collection system
for the used capsules in
Austria (Nespresso
company)
• Pretreatment by the
company Höpperger
Recycling in Pfaffenhofen,
Tyrol, Austria
Pretreatment of used coffee capsules
Co-digestion on WWTP
• Collected capsules
transproted to the central
pretreatment facility in
Tyrol, Austria
• Pretreatment using a
hammer mill
(Wackerbauer, Germany)
• Addition of a liquid
required (washout of the
coffee powder). Liquid
biowaste like whey can be
used
Pretreatment of used coffee capsules
Co-digestion on WWTP
• Produced co-substrate (coffee powder-
whey) transported to the WWTP by a
tank truck (pumpable substrate)
• Storage at the WWTP in a storage tank
• Co-digestion->biogas->CHP->
electricity and heat production
• 300 Nm3 CH4/t dry coffee powder
Digester operation using co-substrates
Co-digestion on WWTP
• Biological stable process (no overloading problems)
• Synergistical enhancement in sewage sludge
methanization, no increase of digestate and disposal
costs up to 25 % co-substrates addition (volatile
solids)
• Most mechanical pretreated biowastes can be stored
without loss of the energy potential
• „New“, anknown digester foaming problems->
research needed! (Known problems with filamentous
bacteria deriving from activted sludge stage)
• Unwanted material (contraries) in the co-susbtrates
(aluminum, glass, sand, plastics etc)
Contraries (impurities) in co-substrates
Co-digestion on WWTP
• Aluminum (coffee capsules), glass, sand, plastics
(biowaste)
• Damage of pumps, clogging of pipes, reduction of the
active, mixed digester volume due to formation of
sediments
• Research topics:
• Quantification of contraries
• Removal of contraries
• Monitoring of the active, mixed digester volume
Contraries (impurities) in co-substrates
Co-digestion on WWTP
• Aluminum (coffee capsules),
glass, sand, plastics (biowaste)
• Damage of pumps, clogging of
pipes, reduction of the active,
mixed digester volume due to
formation of sediments
• Research topics:
• Quantification of contraries
• Monitoring of the active,
mixed digester volume
• Removal of contraries
Contraries (impurities) in co-substrates
Co-digestion on WWTP
• Quantification of contraries
• Sampling
• Extraction of contraries
• Classification, quantification,
size distribution etc.
• Samples taken from sewage
sludge, co-substrates and
• From the digester sediments
(by industry divers)
Contraries (impurities) in co-substrates
Co-digestion on WWTP
• Monitoring of the active, mixed
digester volume
• Important issue for WWTP
• Sensitive tracer method
developed (Volutrack)
• Change of the active, mixed
digester volume can be
monitored
• WWTP Zirl: 1350 m3 original
volume, linear decrease of the
active digester volume (25 m3/a)
• Operational safety, planning and
budgeting of cleaning actions
y = -0,0619x + 3818,6
-
200
400
600
800
1.000
1.200
1.400
01.01.2008 31.12.2009 31.12.2011 30.12.2013 30.12.2015
acti
ve, m
ixe
d d
ige
ste
r vo
lum
e (
m³)
Contraries (impurities) in co-substrates
Co-digestion on WWTP
• Removal of contraries
• Removal from the mechanical pretreated
biowaste difficult due to the high viscosity
(~16 % TS content)
• Dilution of the substrate required
• New idea: Installation of a hydrocyclone in
the external heating circuit
• Internal dilution of the substrate with
digestate ~ 3% dry coffee powder
• Removal of glass, sand etc. in the cyclone
• Prototype installed, promising results
• New research project accepted for further
optimisation of the process
digester content ~ 3 % TS
Co-substrate ~ 16 % TS
heat exchanger
Outlook
Co-digestion on WWTP
• Management of contraries in AD on WWTP, ongoing
projects
• Synergistical effects, enhanced sludge methanisation by
the addition of co-substrates, reduction of disposal costs
for the dewatered sludge
• Serial or parallel operation of the digesters? (degradation
of organic matter, removal of contraries, foam etc.)
• Pre-treatment of substrates and sewage sludge for
enhanced degradation
• Energy storage in the substrate, demand driven
methane/energy production on WWTP
• WWTP as a component in a future, decentralized
energy system based on renewable sources