Environment and Infrastructure
Biogas Technology
Eschborn 07.12.2007
Dishna Schwarz
OE 4413
Environment and Infrastructure
Biogas plant
Environment and Infrastructure
System components of a small biogas plant
or
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Biogas
What is Biogas?
Biogas is a gas produced by anaerobic digestion (in the
absence of oxygen) of organic material, largely comprised of
methane (about two-thirds).
Biogas originates from bacteria in the process of bio-degradation
of organic material under anaerobic (without air) conditions
What is a biodigester?
A biodigester is a tank that processes the organic material that
produces biogas. A biodigester can come in different shapes and
sizes, depending on the needs of the people using it and the local
possibilities in building materials.
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Avantages of anaerobic fermentation
A reliable and simple technology
Many forms of uses from the produced gas (cooking, light,
industrials water heater, combustion engine)
Appropriate technology: individual systems to large production
systems depending on many parameters
A neutral bioenergy for environnement
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A typical biogas system configuration
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Feedstock/Substrate
Animal dung
Fisch waste
Slaughter house waste
Leaves, Water Hyacinth, Banana leaves & stem
Food waste / Market waste
Straw
Municipal Waste( waste water, sludge and solid wastes )
Human exctreta
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Biogas impacts
Energy
– Cooking
– Lighting
– Heating
Saving of fire wood
– Environmental protection through reduced deforestation
– For women: more time for literacy and other income generating activities
Agricultural improvements in terms of plant and animal production yields
– Increased household income
Fertiliser production
- protection and/or recovering of soil fertility
Sanitation
– Controled disposal of animal manure and organic waste
– Greywater collection and reuse
– Improved hygiene and sanitary conditions
Health
– Reduction of diseases related to wastewater and solid waste
– Reduction of exposure to smoke while cooking
Climate protection
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Composition of biogas
Substance Symbol Percentage
Methane CH4 50 - 70
Cabon Dioxide CO2 30 - 40
Hydrogen H2 5 - 10
Nitrogen N2 1-2
Water vapour H2O 0,3
Hydrogen H2S Traces
Sulphide
* Erd gas – 80-90% CH4
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Biogas guideline data
Suitabl digesting temperature 20 – 35°
Retention time 40-100 days
Biogas energy content 6 kWh/m³ = 0.6 l diesel fuel
1 cow yields 9-15 kg dung/d = 0.4m³ gas/d
1 pig yields 2-3 kg dung/d = 0.15 m³ gas/d
gas requirement for cooking 0.1-0.3 m³ /person
1 lamp 0.5 m³ /d ( about 0.13-0.15m³/h )
1 kWh electricity 1 m³ gas
The maximum of biogas production from a given amount of raw material
depends on the type of substrate
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Biogas guideline data
1 Kg firewood => 0.2 m³ biogas
1 Kg dried cow dung => 0.1 m³ biogas
1 Kg Charcoal => 0.5 m³ biogas
1 Litre Kerosine => 2.0 m³ biogas
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Biogas guideline data
8 – 10 m³ biogas plant produces 1.5-2 m³ gas and 100 litres
digested slurry per day using dung from 3-5 cattle or 8-12 pigs.
With that much biogas, a 6-8 person family can:
- cook 2-3 meals
-operate one refrigerator all day
-burn two lamps for 3 hours
-operate a 3 kw motor generator for 1 hour
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Types of biogas plants
Batch type plants are filled and then emptied completely after a
fixed reteition time. They are used for large scale application.High
labour input, gas output not steady.
Continuous plants are fed and emptied continuously.They
empty automatically through the overflow whenever new material
is filled in. They are best suited for small-scale domestic
applications.
If straw and dung are to be digested together , the plant can be
operated on a Semi Batch basis. The slowly digested straw-type
material is fed in about twice a year as a batch load.The dung is
added and removed regularly.
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Types of Biodigesters
Floating Drum
Fixed Dome
Bag Digester
Plastic Digester
Plug Flow Digester
Anaerobic Filter
UASB ( Uplift Anaerobic Sludge Blanket ) Digester
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Fixed dome digester
Fixed dome Chinese model biogas plant as built in China as early
as 1936. It consists of an underground brick masonry
compartment (fermentation chamber) with a dome on the top for
gas storage. In this design, the fermentation chamber and gas
holder are combined as one unit. This design eliminates the use
of costlier mild steel gas holder which is susceptible to corrosion.
The life of fixed dome type plant is longer (from 20 to 50 years) .
Based on the principles of fixed dome model from China, Gobar
Gas and Agricultural Equipment Development Company (GGC) of
Nepal has developed a design and has been popularizing it since
the last 17 years. The concrete dome is the main characteristic of
GGC design .
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Fixed dome digester ( Chinese model )
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Fixed dome plant design
1. Mixing tank with
inlet pipe and sand
trap.
2. Digester.
3. Compensation and
removal tank.
4. Gasholder.
5. Gas pipe.
6. Entry hatch, with
gastight seal.
7. Accumulation of
thick sludge.
Digester Volume VD = SD x RT
(SD = daily substrate input m³/d, 8. Outlet pipe.
RT = rretention time in d ) 9. Reference level.
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Basic function of a fixed-dome biogas plant
1. Mixing pit,
2. Digester,
3. Gasholder,
4. Displacement pit,
5. Gas pipe
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Floating drum digester
Experiment on biogas technology in India began in 1937. In 1956,
Jashu Bhai J Patel developed a design of floating drum biogas
plant popularly known as Gobar Gas plant. In 1962, Patel's
design was approved by the Khadi and Village Industries
Commission (KVIC) of India and this design soon became
popular in India and the world.
In this design, the digester chamber is made of brick masonry in
cement mortar. A mild steel drum is placed on top of the digester
to collect the biogas produced from the digester. Thus, there are
two separate structures for gas production and collection. With
the introduction of fixed dome Chinese model plant, the floating
drum plants became obsolete because of comparatively high
investment and maintenance cost along with other design
weaknesses.
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Floating drum digester ( Indian model )
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Bag digester
This design was developed in 1960s in Taiwan. It consists of a
long cylinder made of PVC or red mud plastic. The bag digester
was developed to solve the problems experienced with brick and
metal digesters. A PVC bag digester was also tested in Nepal by
GGC at Butwal from April to June 1986.
The study concluded that the plastic bag biodigester could be
successful only if PVC bag is easily available, pressure inside the
digester is increased and welding facilities are easily available.
Such conditions are difficult to meet in most of the rural areas in
developing countries.
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Bag Digester
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Plug flow digester
The plug flow digester is similar to the bag digester. It consists of
a trench (trench length has to be considerably greater than the
width and depth) lined with concrete or an impermeable
membrane. The reactor is covered with either a flexible cover gas
holder anchored to the ground, concrete or galvanized iron (GI)
top. The first documented use of this type of design was in South
Africa in 1957
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Plug flow digester
Plug-flow digesters are suitable for ruminant animal manure that has a solids
concentration of 11 percent to 13 percent. New material added to the tank at
one end pushes older material to the opposite end. Coarse solids in ruminant
Manure form a viscous material as they are digested, limiting solids separation
in the digester tank. As a result, the material flows through the tank in a "plug.„
Average retention time (the time a manure "plug" remains in the digester)
is 20 to 30 days.
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Plugflow digester model
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Anaerobic filter
This type of digester was developed in the 1950's to use relatively
dilute and soluble waste water with low level of suspended solids.
It is one of the earliest and simplest type of design developed to
reduce the reactor volume. It consists of a column filled with a
packing medium. A great variety of non-biodegradable materials
have been used as packing media for anaerobic filter reactors
such as stones, plastic, coral, mussel shells, reeds, and bamboo
rings. The methane forming bacteria form a film on the large
surface of the packing medium and are not carried out of the
digester with the effluent. For this reason, these reactors are also
known as "fixed film" or "retained film" digesters
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Upflow anaerobic sludge blanket –UASB plants
This UASB design was developed in 1980 in the Netherlands. It is
similar to the anaerobic filter in that it involves a high
concentration of immobilized bacteria in the reactor. However, the
UASB reactors contain no packing medium, instead, the methane
forming bacteria are concentrated in the dense granules of sludge
blanket which covers the lower part of the reactor. The feed liquid
enters from the bottom of the reactor and biogas is produced
while liquid flows up through the sludge blanket. Many full-scale
UASB plants are in operation in Europe using wastewater from
sugar beet processing and other dilute wastes that contain mainly
soluble carbohydrates.
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UASB plant
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Parameters for process optimisation
Substrate temparature
Available nutrients
Retention time ( flow through time )
PH level
Nitrogen inhibition and C/N ratio
Substrate solid content and agitation
Inhibitory factors
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Substrate temperature
Temperature range of anaerobic fermentation
Anaerobic fermentation is in principle possible between 3°C and
approximately 70°C. Differentiation is generally made between
three temperature ranges:
The psychrophilic temperature range lies below 20°C
the mesophilic temperature range between 20°C and 40°C
the thermophilic temperature range between 40°C and 55 °C
Ideal temparature 20 °C – 28°C
If the temperature of the bio-mass is below 15°C, gas production
will be so low that the biogas plant is no longer economically
feasible.
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Available nutrient
In order to grow, bacteria need more than just a supply of organic
substances as a source of carbon and energy
Requires an adequate supply of nitrogen, sulfur, phosphorous,
potassium, calcium, magnesium and a number of trace elements
such as iron, manganese, molybdenum, zinc, cobalt, selenium,
tungsten, nickel etc
"Normal" substrates such as agricultural residues or municipal
sewage usually contain adequate amounts of the mentioned
elements.
Higher concentration of any individual substance usually has an
inhibitory effect, so that analyses are recommended on a case-to-
case basis to determine which amount of which nutrients, if any,
still needs to be added.
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Retention time
can only be accurately defined in batch-type facilities. For
continuous systems, the mean retention time is approximated by
dividing the digester volume by the daily influent rate.
Depending on the vessel geometry, the means of mixing, etc., the
effective retention time may vary widely for the individual
substrate constituents.
Selection of a suitable retention time thus depends not only on
the process temperature, but also on the type of substrate used.
Substrate
For liquid manure undergoing fermentation in the mesophilic
temperature range, the following approximate values apply:
liquid cow manure: 20-30 days
liquid pig manure: 15-25 days
liquid chicken manure: 20-40 days
animal manure mixed with plant material: 50-80 days
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Gas production vs retention time
1,4
1,2 at 15º
at 25º
Specific gas production (l/l/d)
1
at 35º
0,8
0,6
0,4
0,2
0
1 5 9 13 17 21 25 29 33 37
Tim e of digestion (days)
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PH value
The methane-producing bacteria live best under neutral to slightly
alkaline conditions. Once the process of fermentation has
stabilized under anaerobic conditions, the pH will normally take
on a value of between 7 and 8.5.
If the pH value drops below 6.2, the medium will have a toxic
effect on the methanogenic bacteria.
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Nitrogen-content and C/N-ratio of organic substrates
Biodegradable N(%) C/N
material
metabolic activity of
Night Soil 6.0 5.9-10 methanogenic
Cow manure 1.7 16.6-25 bacteria can be
optimized at a C/N
Pig manure 3.8 6.2-12.5
ratio of approximately
Chicken dropings 6.3 5-7.1 8-20, whereby the
optimum point varies
Hay 4.0 12.5-25
from case to case,
Water hyacinth 2.9 11.4 depending on the
Kitchen waste 1.9 28.60 nature of the
substrate.
Rice straw 0.6 67
Bagasse 0.3 150 Substrate can be
Fallen leaves 1.0 50 mixed to get the
optimum C/N ratio
Sea weed 1.9 79
Sawdust 0.1 200 - 500
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Substrate agitation
Agitation
different ways of homogenising the substrate or mixing it with
water and co-substrate
Mixing and homogenizing the substrate in the mixing chamber
Agitation inside the digester
Poking through the in- and outlet pipes (small scale plants)
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Solids content
Dry solid matter
Substrate after the withdrawal of water
For AD suitable solid waste range : 10 % - 40%
Organic dry solid matter content
Organic share of the dry matter ( for anaerobic digestion it should exceed
50% )
Structure material
Substrate with high content of lignin- a type of carbon - ( wood, shrub/tree
cut offs )
Low content : advantageous for AD
High : Composting
Toxic substances
Hinder digestion process
Should be kept low
Protein content
Should not exceed 50%
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Inhibitory factors
The presence of heavy metals, antibiotics and detergents used in
livestock husbandry can have an inhibitory effect on the process
of bio-methanation.
The following table lists the limit concentrations (mg/l) for various
inhibitors.
Substance [mg/l]
Copper 10-250
Calcium 8000
Sodium 8000
Magnesium 3000
Nickel 100-1000
Zinc 350-1000
Chromium 200-2000
Sulfide (as Sulfur) 200
Cyanide 2
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Biogas appliances – small scale
Domestic plants
Gas cookers
Gas Lamps
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Gas cookers
basic requirements:
simple and easy operation
versatility, e.g. for pots of various size, for cooking and broiling
easy to clean
acceptable cost and easy repair
good burning properties, i.e. stable flame, high efficiency
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Biogas lamps
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Biogas lamps
Not very efficient
Get very hot
Mantel last not long
Gas & air should be properly mixed before entering the mantel -
biogas lamps are controlled by adjusting the supply of gas and
primary air. The aim is to make the gas mantle burn with uniform
brightness and a steady,
Less lumen output
1 lamp needs ca 120 – 150 L /day
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Options of biogas utilisation
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Options of biogas utilisation
Gas-engine electricity generation needs medium-grade biogas
purification (removal of moisture and trace gases)
Biogas needs to be high-graded with carbon-dioxide removal to
natural gas standards
Utilisation of biogas for vehicles needs high-upgraded biogas
with a quality compared to LNG/CNG
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Biogas as a sanitation option- Ecosan concept
Human excreta from dry or low flush toilets and biodegradable
organic fraction of household waste could enter a (on-site or off-
site) anaerobic (wet or dry) digester to be treated and to produce
biogas
The concentration of nitrogen in the black water could be so high,
that the digestion process could be stopped. Ammonia from the
urine will be transformed by enzymes in urea, carbon dioxide and
ammoniac. Urea will be toxic to the bacteria (self-intoxification).
Solution : Urin separation
from an energy point of view, its better to have some animal
manure or additional feed of organic waste to optimize the
retention time / construction volume related to energy output
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Composition of household wastewater
20
14.1
12.3
6
5.3
3.6
K
P
Organics
0 kg COD/ (Person·year)
N
10.000 – 200.000 l
0.8 1.0
Nutrient content
0 kg N,P,K / (Person·year)
Volume
Liter / (Person·year)
greywater urine faeces
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urine Grey water
faeces rainwater organic waste
(shower,
Substances (yellow water) (brown water)
washing, etc.)
manure
anaerobic constructed
composting,
hygienisation by wetlands, gardening, filtration,
Treatment storage or
digestion,
wastewater ponds, biol. biological
anaerobic
drying, digestion
drying treatment, membrane- treatment
composting
technology
irrigation, soil
biogas, water supply,
liquid or dry groundwater- improvement,
soil groundwater-
utilisation fertiliser
improvement
recharge or
recharge
biogas
direct reuse
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Anaerobic treatment with biogas production
small-scale biogas plants:
decentralized treatment of household
wastewater with or without agricultural
waste
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Biogas from wastewater systems
Material
Inlet
Irrigation
Gas pipe
Methan production by
methanogenic micro-
organisms
Water storage for
Constructed wetlands for irrigation
sludge treatment
Effluent outlet
Biodigestor replacing septic tank . Waste water and domestic waste are treated and transformed into biogas,
sludge et water.
Advantages: no work requested to empty septic tanks, waste reuse for energy, fertilizer, irrigation water,
cash flow saving
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Chinese „four in one“ model
pig – toilet – biogas – vegetable
combined with Greenhouse Production
more than 1,000,000 times in peri-urban areas
of Megacities in Northern China .
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Navsarjan Trust ecosan pilot project – DSK, India
construction of the night-soil based biogas plant
inlet chamber for
toilet water
biogasreactor in the center
of the building
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Adarsh Vidya Mandir school, Badlapur, India
sketch of the three storeyed sanitation block
urinals for men and women: urin to collection tanks (fertilizer)
ladies
pour flush toilets: black water to biogas plant (gas for cooking)
water to constructed wetlands
(for irrigation purpose)
gents
hand wash facilities: greywater to greywater gardens (irigation)
biogas plant wetlands
blackwater
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Biogas from household wastewater - China
137,000 community biogas septic tanks
(DEWATS) for purification of household
wastewater with more than 0.5 billion
tons of wastewater treated annually
Septic tanks
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System components of a wastewater biogas plant
max
min
Sludge stabilization and separation tank
Biogas tank
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GTZ biogas experiences
In the Past
In 1970 s first trials with the technology
1983-1990 Biogas extension service
1988 & 1992 - Biogas survey with BORDA
1992 – 1994 SEP biogas components
1996 - promotion of Anaerobic Technology for the Treatment of municipal
and industrial wastewater ( experiences and recommendations from more
than 20 countries have been analysed and documented
1996 – 2006 GATE biogas information service and biogas homepage
On going
Ecosan biogas projects
Some PPP projects
Future
„Biogas for a better life „ ( feasibility studies for Tanzania & Burkina Faso )
?????
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GTZ - Biogas experiences in Africa
• East Africa
Kenya, Tanzania, Ethiopia ( first
GTZ -biogas project in 1977 )
• West Africa
Burkina Faso, Ivory coast, Mali
• Central Africa
Cameroon, Burundi, Rwanda
• North Africa
Morrocco, Tunisia
• South Africa
Lesotho
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Number of biogas plants installed
Country Pilot plants/ Dissemination projects/
Number of plants Number of plants
Burkina Faso 6
Burundi over 300
Cameroon 43
Ethiopia over 100
Kenya over 300
Lesotho 65
Mali 34
Morocco over 100
Ivory Coast 80
Rwanda 2 large plants
Tanzania over 300
Tunisia 30
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Das BIOTECH model India – 2007 Ashden Award 1. prize winner
12000 domestic plants
160 with latrine connection
220 institutional plants
17 municipal plants
Feedstock : food waste/market
waste
Small domestic plants gives 1 -2
hrs gas for cooking
Households replace about 30%
of LPG or about 44 kg per year,
saving Rs1,200 per year
Municipal plants generate
electricity for the markets
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Das SKG Sangha model India – 2007 Ashden Award 2.prize winner
43,000 household plants
vermi-composting system
(mixing the slurry with solid
waste -straw, green and dried
leaves )
save about 4 tonnes/year of
CO2 and around 3.5
tonnes/year of fuel wood.
200 bags of vermiculture
manure a year ,
earning Rs90 (1,20€) for a 30kg
bag
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Das ARTI model Indien- Ashden prize winner 2006
700 household plants
Digester and the gas holder
made out of recycled plastic
( water tanks available in the
market – 1m³ and 0.75m³)
Needs only 1 Kg feedstock
for 500 litres of biogas
Quick digestion process ( 48
hrs instead of 40 days )
Feedstock: food waste, rotten
fruit,spoilt milk and grains, oil
cake
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Biogas plant Galha - Srilanka
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Biogas plant GSS – Galaha Srilank
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Biogas plant Galaha - Srilanka
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Biogas plant GSS - Galaha Srilanka
Vegetable garden and composting
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Biogas plant GSS – Galaha Srilanka -
Vegetable Garden
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Biogas plant GSS- Galaha Srilanka
Gas cooker
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Biogas plant Bawlana Srilanka
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Biogas plant Bawlana Srilanka
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Biogas plant –Masgolla Srilanka
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Biogas plant Masgolla Srilanka
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Biogas situation in Germany
Basic Facts
Average size of the plants – 350 kw
Many 150 Kw plants in agricultural sector
Few 550 Kw plants in 2006/2007
Most of the plants are concentrated in Bavaria
850 plants in 1999, 3280 in plants 2006, 3900 plants in 2007
1300 MW in 2007
Gas utilisation
to produce electric and thermal energy ( BHKW )
( efficiency electric 28-38% , thermal 42-58% )
20 – 40% of the thermal energy gained is required maintain the
process temparature in the digester .
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Biogas plants in Germany
4000
3500
3000
2500
2000
No of plants
1500
1000
500
0
1999 2001 2003 2005 2007
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Biogas plants in Germany . Energy production
1400
1200
1000
800
600 MW
400
200
0
1999 2001 2003 2005 2007
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Large scale biogas plant Germany
Flow chart ( farm )
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Large scale biogas plant Germany
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Stromvergütung
Stromvergütung nach Erneuerbare Energien Gesetz (EEG), dessen
Neuerung am 01.08.2004 in Kraft trat beträgt für Biogasanlagen, die
nach dem 31.12.2004 erstmals einspeisen wie folgt:
bis einschließlich einer Leistung von 150 kW mindestens 11,3
Cent/kWh elektr.
bis einschließlich einer Leistung von 500 kW mindestens 9,7
Cent/kWh elektr.
bis einschließlich einer Leistung von 5.000 kW mindestens 8,7
Cent/kWh elektr.
Empfehlung für die Zukunft: Verringerung der Grundvergütung um 0,
50 Cent, Erhöhung der Prämie für die Kraft-Wärme-Kopplung um 1
Cent
Biogasanlagen in Deutschland müssen ungefähr eine Leistung
von 600 -700 KW erbringen um rentable zu sein
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Successful biogas programs
BSP Nepal from 1992 – to date
existing design, fixed dome 4³ – 10m³ subsidy , giant PR
campaigns, government involvement in all policy decisions, yearly
user satisfaction survey, systematic after sales services, upto now
165 plants , use only for cooking
TED biogas project Lesotho from 2003 – to date)
modified DATWAS system, fixed dome 8m³ - 32m ³, no subsidy,
marginal government involvement,upto now 80 plants on
demand, final guarantee service, use multiple
Biogas projects in India & China ( different concepts & models )
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BSP Nepal
upto now 165.000 plants
existing design, GC 2047 , fixed dome 4³ – 10m³
subsidy
giant PR campaigns through radio, TV, booklets etc
government involvement in all levels of policy decisions
yearly user satisfaction survey
systematic after sales services
Target group households with minimum requirements
gas only for cooking
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Progress of the biogas plant construction – BSP Nepal
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Current subsidy flow – BSP Nepal
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Institutional set up – BSP Nepal
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National implementation structure BSP-Nepal
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Calculation example – BSP Nepal – 8 m³ plant
Costs in NRP
Capital costs 26,070
Annual maintenance costs 261 - 1 % of capital costs
Subsidy 10,000
Net costs 16,070
Down payment 1,607 - 10% of net costs
Loan amount 14,463
Annual loan payment 3,687 - 17% interest, 7 years term
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MAIN SUCCESS FACTORS – BSP Nepal
Integrated farming system, which combines crop production
and animal husbandry.
Supportive government policy
Long-term donor commitment
Collaboration between international organisations
Carefully defined quality and design standards
Guarantee of after sales service
Transparency in the implementation of the program
Uniform technology - the fixed dome biogas digester
Farmer-to farmer promotion to friends and neighbours about
the benefits
Institutional development and strengthening
Capacity building
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Biogas in Lesotho
So far only 80 fixed dome plants ( DEWATS -
Decentralised Wastewater Treatment Systems )
Digester also serves as on-site sanitation solution and replaces
malfunctioning septic tanks
TED's construction activities are completely demand driven and
not subsidized
never a proper definition of a target group. The interested
customers are those who feel they have a problem especially with
their sewage
Interested individuals and groups frequently visit the first site
where a biogas plant is constructed
TED advertises with all means available within the daily context
and not expensive
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Main success factors- TED biogas plants Lesotho
The core of the technology is mature
The execution of the work gives high priority to quality
The technological set up offered solves a problem that the
people really feel and has impacted on their pocket
A customer has to actively demand the technology
Potential customers see an example of the technology in the
negotiation phase
Many avenues in the daily context are used for advertisement
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Launching biogas programmes
Excluding factors
Too cold or too dry region
Irregular or no gas demand
Less than 20 kg dung/day available
No stabling or livestock in large pens where dung cannot be
collected
No building materials available locally
Integration of the biogas plant into the household and farm
routines not possible
No suitable institution can be found for dissemination
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Launching biogas programmes
Critical factors
low income or unstable economic situation f the target group
Good energy supply through the year
Gas appliances not available regionally or nationally
High building costs
No substantial interest of the government is evident over the
medium term
Counterpart organisation has only indirect access to the target
group
Low qualification of maisons/ technicians
Unfavourable macro and microeconomic coefficients
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Launching biogas programmes
Ideal factors
Daily temparatures over 20° throughout the year
Regular gas demand
Full stabling of animals ( on solid floors as far as possible )
At least 30 kg / day dung available per plant
Dairy farming
Use of organic fertiliser is normal
Insufficient supply of fossile sources of energy
Efficient counterpart organisations with the ability of cooperating with the
private sector
Political will ( government ) towards biogas technology as well as
strengthening small and medium scale farm systems
Secured financing of the dissemination structure
Gas utilisation and attendance of the plant can be clearly regulated within
the household
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GHG emission reduction potential of domestic
Biogas installations
depends mainly on the:
local situation
size and the way the installation is operated
GHG reduction range of 1.7* to 7** tons CO2eq per installation
per year is possible.
* Tentative calculations for Nepal, based on proposed methodology 1E.
** Current claim by Cambodia Biogas Programme for HIVOS voluntary market.
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Biogas and GHG reduction potential
CER - certified emission reductions
VER – verified emission reductions ( voluntary market – less
standardized and suitable for small scale projects
Projects below 15,000 tCO2eq per year are fee exempted, US$ 0.10 and US$20
per CER will be due for issued CERs up to 15,000 tCO2eq and over 15,000
tCO2eq respectively, with a maximum of US$ 350,000
Environment and Infrastructure
Biogas and GHG reduction
Biogas & GHG reduction
Manure Fossil- and Chemical
handling NRB fuel fertilizer
modality substitution substitution
Environment and Infrastructure
Biogas and CDM
Emission trading under the CDM
Environment and Infrastructure
Biogas and CDM
CDM project activity cycle
Environment and Infrastructure
Biogas and CDM
Project expenses and carbon revenue
800
700
Carbon revenue
600 Carbon rebate
Support
500
Investment
Euro
400
300
200
100
0
Expenses Carbon revenue
Environment and Infrastructure
Biogas and CDM
Environment and Infrastructure
Launching biogas programmes
Lessons lerned
Long term programmes are needed for market development and
dissemination of the technology
Investment subsidy and credits on reasonable terms necessary ( use and
strengthen existing finance institutes and programmes )
Appropriate technology (fixed dome plants are suitable for many African
countries ) and make the technology cheaper and affordable for poor
households ( introduce new technologies )
Offer standardised plants for selection ( 6m³, 10m³ , 15m³ etc. ) and
define quality standards
Provide capacity building and awareness raising for all actors involved
( governments, engineers/technicians, banks, private sector, masons,
farmers/households )
Support to create local market structures/business development to deal
with construction materials, gas appliances and spare parts etc.
Environment and Infrastructure
Launching biogas programmes
Failures
Biogas plant is still an expensive energy option for many rural
households
Lack of government commitment and suitable market structure to develop
a sustainable dissemination of the technology
Bad experiences and poor image created by many failed biogas plants
No feed material/water available continuously (low gas production )
Poor design/construction ( gas leakages ), wrong operation and lack of
maintenance services
Gas appliances and spare parts are not available in the local market
Cooking habits ( fuel wood and kerosene are preferred to prepare
traditional food ) and farming practises ( refuse to use organic fertilizer )
Environment and Infrastructure
Launching biogas programmes
Success factors
Strong government commitment and private sector involvement
Appropriate financing mechanisms for poor households
High quality construction work
Low price of plant in relation to the income of the target group
Acceptance of the technology ( gas as energy source for cooking and
lighting, slurry as fertilizer )
Households/farmers re trained in the proper use/operation of biogas
plants
Skilled engineers/technicians and masons
Reliable and professional construction / after sales service
Efficient counterpart organisations with the possibility of cooperating with
the private sector
willingness among potential users to handle animal dung and to attach a
toilet to the plant
Environment and Infrastructure
Favourable conditions to setup biogas programs
technology corresponds to the geographic, economic and
particularly the agricultural framework
Scarcity of traditional cooking fuels
Government involvement incentives or subsidies for energy from RE
Long term programmes -at least 5 years
Access to credits under attractive conditions or subsidies on
material
Potential biogas customers are scattered through out the region
Adequate maintenance/repair service
Qualification, mainly of the mason
local availability of suitable building materials
Availability of gas appliances and spare parts
Standard sizes of biogas plants ( 6 m³, 8 m³ etc. )
Environment and Infrastructure
Necessary actions for setting up biogas Implementation
Programmes
In depth analysis of favourable conditions to initiate national biogas
programmes ( water, climate, density of households/farms, size of the
farm, household energy consumption patterns, availability of construction
materials, skilled man power etc ).
Market research on available energy sources and substitutes, economic
benefits, social acceptance, technological viability and sustainability
Check on government incentives or subsidies for energy from renewable
energy sources, potential of local entrepreneurs
Research on available designs and appliances according to the specific
regional conditions
Study on recent developments and new approaches
Awareness raising and promotion campaigns