Optimising the Anaerobic Digestion Process · 2011-09-14 · 1 Table of contents 1. Examining the...
Transcript of Optimising the Anaerobic Digestion Process · 2011-09-14 · 1 Table of contents 1. Examining the...
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Optimizing the Anaerobic Digestion Process
Examining the different types of
anaerobic digestion technologies
Frank Hofmann
7th September 2011, South Baltic Gas Forum, Gdansk
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Table of contents
1. Examining the different types of anaerobic digestion technologies
� Completely stirred reactor
� Plug-flow reactor
� Batch wise operated systems
� Lagoon biogas plants
� Specialized reactors (like UASB, dry fermentation)
2. Advanced biogas utilization
� Biogas upgrading
� Injection in the gas grid
� Use for transportation purposes
� CHP integration and optimization
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Examining the different types of anaerobic digestion technologies
Completely stirred reactor
Source: Ecofys
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Completely stirred reactor I
Opportunities for optimization (biochemical process)
� Mesophilic – thermophilic conditions
� Separated stages
� Stages in a row - parallel
� External hydrolysis
� Biochemical optimization
� Enzymes
� Minerals
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Completely stirred reactor II
Opportunities for optimization (technology)
� Gas yield
� Energy demand
� Operational hours
� Process
� Technology
� Efficient energy utilization
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Completely stirred reactor III
Gas yield
� Pre treatment of biomass
� Example: Thermo-pressure-hydrolysis
� >190°C
� 20 min
� Decomposition of long carbon hydrates
� Reduced retention time
� Higher gas yield
� Sanitation of the material
� Option to treat material that is more difficult to degrade (cheaper feedstock, like straw, sewage sludge)
� Combination with thermophilic digestion
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Completely stirred reactor IV, electricity demand
n=297
0
10
20
30
40
50
10 100 1.000 10.000
installierte Leistung [kWel]
Eig
enstr
om
bedarf
[%
]
Installed electrical capacity [kWel]
Ownelectricitydemand[%
of production]
Source: DBFZ
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Completely stirred reactor V, disturbances
Operational hours
Source: Weiland et. al. (2008): Biology: 5th main reason for disturbancesDBFZ
Relative frequency Working efforts
Wo
rkin
geff
ort
sh
ou
rsp
er
week
Rela
tive f
req
uen
cy
of
dis
turb
an
ces
in %
Waste
in
pu
tte
ch
no
log
ies
Mech
an
ical
Pre
treatm
en
t
Sep
ara
tio
n
of
imp
uri
ties
Hyg
ien
isati
on
Bio
log
ical
Pro
cess
Pu
mp
s
So
lid
su
bstr
ate
Feed
ing
Sti
rrin
g
Clo
gg
ing
s
Gas p
uri
ficati
on
CH
P u
nit
Co
ntr
ol
eq
uip
men
t
Gas lo
sses
Oth
ers
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Completely stirred reactor VI, CHP
Source: Weiland et. al. (2008) and DBFZ
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Cumulated annual standstill of CHP units in 60 German biogas plants [d/a]
Re
lati
ve f
req
uen
cy
[%]
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Completely stirred reactor VII, heat utilization
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n=166
0
20
40
60
80
100
≤ 50 51 - 150 151 - 500 501 – 1.000 > 1.000
installierte elektr. Anlagenleistung [kWel]
Ante
il B
iogasanla
gen m
it ents
pre
chenden
Wärm
enutz
ungsgra
d [%
]
Biogasanlagen Wärmenutzungsgrad ≤50% [%] Biogasanlagen Wärmenutzungsgrad >50% [%]
Share
of pla
nts
with
giv
en
heat
utliz
ation
share
[%]
Installed electrical capacity [kWel]
Average heat utilization share < 50 % Average heat utilization share > 50 %
Source: DBFZ
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Other types of anaerobic digestion technologies
� Lagoon biogas plants
� Specialized reactors like
� UASB
� Plug flow digestion
� Dry fermentation
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Lagoon systems for (industrial) waste water
Source: Ecofys
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Reasons for Lagoon systems
� Relatively cheap investment costs
� Huge amount of water processable
� Energy production
� COD/BOD reduction
� Waste stabilization (pH, volatiles, vector attraction)
� Odour reduction
� Immobilization of Heavy Metals (sulphide binds heavy metals)
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Chemical oxygen demand, COD
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Examples of input material,COD
� Meat, dairy processing, beer, winery, sugar beet, starch 5-10 kg/m3
� Ethanol vinasse 28-31 kg/m3
� Piggery effluent 10-30 kg/m3
� POME, wool processing 50-100 kg/m3
� Distillery slops 40-200 kg/m3
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Best Project Checklist
� Site conditions
� Size: large volumes of waste (water)
� Waste strength & composition
(Biodegradability)
� Waste temperature
� Open lagoon emissions
� Climate conditions
� Processing season
� Energy demand by owner
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Waste composition (Biodegradability)
� Simple wastewaters (soluble):
� Sugar, soft-drink, beer/wine, vinasse, blanching/cannery, some pharmaceutical, chemical
� Complex wastewaters (fat, protein)
� Slaughterhouse, dairy, starch, POME, wool, fish
� ‘Difficult’ wastewater
� Pulp and paper, rendering, tannery, distillery slops
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Conclusions Lagoon systems
� Opportunities in agro-industry, palm oil, starch, ethanol, food processing, slaughterhouse waste, dairy waste, solid waste and many more
� Processes depending on waste and location
� Lagoon-based treatment is best practical option for wastewaters containing suspended solids, fats and/or proteins in areas where space availability is not a problem
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UASB technology
� Process / waste water treatment
� High investment costs
� Low space requirement
Source: Ecofys
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Operating principle of plug-flow digestion.
Kompogas system
Strabag-system
Source: Kompogas
Source: Strabag
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Combination of plug flow, thermal treatment and completely mixed reactors
System as developed by Company Eisenmann
Source: Eisenmann AG
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Dry fermentation
� Input material often > 25 %
� Moderate to high investment costs
� No need for pre-treatment and stable process
Biogas Plant München – Source: Bekon GmbH & Co K.G.
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Operating principle of batch wise digestion
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Upgraded Biogas
Source: Deutsches BiomasseForschungsZentrum gGmbH
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Overview: utilisation of biogas
Upgrading and feeding biogas into the natural gas grid offers the possibility to use the upgraded biogas at the location of demand for electricity, heat, cold or fuel.
Source: Ecofys
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Differences between biogas and natural H-gas
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Upgrading technologies for biogas
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• 41 running plants with about 25,000 m³/h biomethane
• Largest: 5,300 m³/h biomethane
• Mainly 4 Technologies
0
10
20
30
40
50
60
2005 2006 2007 2008 2009 2010*
An
lag
en
za
hl
[-]
0
5000
10000
15000
20000
25000
30000
35000
Au
fbe
reit
un
gs
ka
pa
zit
ät
Bio
me
tha
n
[Nm
³/h
]Schätzung Zubau 2.HJ
Anlagenzahl
Aufbereitungskapazität [Nm³/h]
Biogas upgrading in Germany
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Biogas feed-in capacity in Europe sorted according to countries
Sources: dena, ISET, DVGW e.V.
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Conclusions biogas upgrading and gas grid connection
�The overall feed-in capacity of all European biogas feed-in projects in operation currently amounts to 28,000 Nm³/h or about 150 MW
�Locations: Sweden, Switzerland, Netherlands, France, Germany
�Main utilization as gas grid injection or car fuel
�Legal frameworks were responsible for the development in the mentioned countries
�In Europe ~8 technology suppliers of upgrading biogas technology
�Main technologies are pressurized water scrubbing, pressurizes swing absorption, chemical (water) scrubbing and membrane separation
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Gas utilisation, CHP and alternatives
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Combined Heat and Power (CHP)
� Application in Gen-Sets with adapted gas or diesel engines for electricity and heat production
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� Fuel Cell
� � el. efficiency is up to 48% (55%);
� 1 pilot plant in service, still quite expensive
� ORC-Modules
� converting waste heat into electricity� 10% raise in el. efficiency; 3 plants in operation,
� Is additional to standard gas engine if heat is not utilized otherwise
� Micro gas turbines
�less sensitive, low maintenance costs, high durability
�compared to gas engines low el. efficiency
(38% � 28%)
Source: Köhler & Ziegler
Source: MTU
Source: ISET
Electricity generation,
other technologies
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Summary I
�Biogas plants are state of the art technologies
�There has been a huge technical development in the last 10 years
�Optimizing potentials are in the
� biochemical process
� Reliability of the technology
�There are very different kind of AD technologies on the market which are adapted on the special biomass
�Most efficient gas utilization is still a challenge
� Annual operation time
� Heat utilization
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Summary II
�There are very different types of biogas technologies on the market, optimized for different boundary conditions
�Biowaste treatment plants have a huge potential and some special advantages.
�Lagoon biogas systems have an enormous potential and are relatively cheap
�By biogas upgrading to natural gas quality the gas utilization can be enlarged
�Biogas production is also important as part of the chain in biofuel production, particularly for second generation biofuels:
� Conversion of the wet by-product from fermentation;
� Supply of heat and electricity for the ethanol distillation;
� Conversion of glycerin, by product of biodiesel production
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Please contact us for more information
Ecofys Germany GmbH
Stralauer Platz 34
10243 Berlin
Germany
Frank Hofmann
T: +49 (0) 30 2977 3579 41
W: www.ecofys.de