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Proceedings of the Second International Seminar on Theoretical Physics & National
Development, 5-8 July, 2009, Abuja, Nigeria
280
TECHNO-ECONOMIC ANALYSIS OF A BIOGAS PLANT FOR AGRICULTURAL
APPLICATIONS; A CASE STUDY OF CONCORDIA FARMS LTD, PORTHARCOURT†
Torbira-Lenee, Mtamabari Simeon
Department of Mechanical Engineering, University of Nigeria, Nsukka, Nigeria.
e-mail:[email protected]
Abstract
A techno-economic analysis of generating biogas using a fixed dome
digester coupled with a solar collector through a heat exchanger has been
studied for Concordia Farms Limited. This gas when generated from
organic waste on the farm could replace power-generating plant in the farm
and save the huge cost (in naira) consumed by the private power plant in
generating energy for the farm. Mathematical computations have been
made to optimize different analysis, namely; organic waste generating
capacity of the farms, volume of digester suitable for the farm, energy
requirements/needs of the farm, available energy sources of the farm and its
biogas generating potentials. The design criteria for thermal heating of an
active, fixed-dome type biogas plant is presented with the effects of heat
exchanger and collector panel incorporated in the thermal analysis.
Increasing the flow rate of the working fluid between the heat exchanger
and the collector loop can optimize the thermal efficiency. The economic
analysis takes into account, capital and maintenance costs, life of the
project, priced and unpriced benefits of owning a biogas plant. Priced
benefits involves cost valuation (in naira) of the various fuels used e.g. fuel
wood, kerosene, PMS, diesel and time and labour etc. which becomes the
cost saved/avoided by owning a biogas plant. The benefit – cost ratio,
internal rate of returns and net present values, cost-payback and energy
† African Journal of Physics Vol. 2, 280-299, (2009)
ISSN: PRINT: 1948-0229 CD ROM:1948-0245 ONLINE: 1948-0237
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payback of the investment are also computed to establish the viability of the
proposed biogas project.
1.0 INTRODUCTION
The energy crisis in the early 70’s caused economic problems for many
countries that depend on imported oil and gases. With the high cost and instability
in the price, non-renewability of petroleum products as well as the growing
environmental concern (global warming) on burning of fossil fuels, the need for a
renewable and more environmentally friendly fuel has become imperative. The
exploitation of new energy sources and the adoption of new energy conversion
technologies became necessary towards reduction of enormous organic waste
generated especially in the integrated farms and providing an alternative,
environment compatible, cheap source of renewable energy for such farms – in
Nigeria. Huge quantities of organic waste running into several hundreds of tons
are generated in integrated farms a year. At the same time, these farms spent huge
sums of money on electricity bills, operating private power generating plants, fuel
wood, kerosene, etc. to meet energy needs of farm.
Biogas (also called “Marsh gas”), a by-product of anaerobic decomposition
of organic waste has been considered as an alternative source of energy. Wiley
(1996) noted that the common raw materials for biogas generation are often
defined as “waste materials”, e.g. animal manure, sewage sludge and vegetable
crop residues, all of which are rich in nutrients suitable for the growth of
anaerobic bacteria.
The interest in the present paper is therefore to produce biogas from animal
dungs generated on the this farm that can be used as a cheap, renewable source of
energy on the farm. It is also the aim of this work to compare the cost of owning a
owning a biogas plant by the farm with that of buying fossil fuels.
2. METHODOLOGIES AND MATERIALS
This project was conducted by using a triangulation method consisting of:
literature review, background research/case studies and direct interviews. The
literature review and background research provides an initial overview of biogas.
These sources described what biogas is, how it is produced, and how it could be
used. The literature review transcribed what studies have been done in reference
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to biogas and current projects using biogas technology. To increase the validity of
the project, only recent journal articles were reviewed.
Background research and case studies were reviewed and will serve as a
comparison to the potential Concordia farms project and provide information as to
the size, capacity, and type of biogas plant that would best suit Concordia farms
limited. Interviews were conducted to several local farm workers about organic
wastes including farmers, farm manager, and farm equipment
operators/maintenance workers, and marketers. The verbal interview questions
were reviewed and passed by Concordia farms Office of Research Ethics.
Approval from the Research Ethics office was needed to interview the manager
and farmers. Interview participants were selected from criteria, which were based
on the proximity of the participants to the farm, and the volume of wastes that
could be generated. Maximum waste could be collected from such farm as
compared to slaughters’ wastes. Participants were contacted directly.
Series of questions were asked regarding where the waste goes currently,
farms sources of energy, farm’s cost on energy, energy needs of the farm and
whether they would be willing to donate their organic waste if a biogas plant is
built on the farm for biogas generation, and the sludge used as manure in
agriculture. The collected data was taken and assessed to determine extra amounts
of organic waste needed for the biogas plant. The economic feasibility of the
biogas plant was conducted with all data collected. This was be followed by a
discussion, recommendations and alternatives for the feasibility of this project.
This method of triangulation attempts to use the most recent and innovative
technologies to minimize potential operational and start-up problems. This
method also emphasizes the benefits a biogas operation would have on the local
community and Concordia farms limited
The farms have the following number of animals and poultry as sources of
dung generation for biogas; 3500 – Birds, 400 – Pigs, 200 – Sheep, 300 – Cows
The type, quantity, and cost of energy consumed per month by the farm are as
follows;
- Fuel wood 20,000kg/month N128, 000.00
- Kerosene 7000 litres/month N330, 750.00
- Diesel 10,000 litres/month N542, 750.00
- P.M.S 10,000 litres/month N514, 000.00
- Charcoal 3500kg/month N8, 750.00
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3. OBJECTIVE OF THE STUDY
To provide an alternative source of energy to the farm hence reduce its over
dependency on fossil fuels
-To produce a cheap, environmentally friendly energy for the farm use
To convert the huge organic waste generated on the farm into useful energy
hence enhancing good farm hygiene and reducing expenses on fossil fuels
To increase farm outputs and reduce inputs
To integrate biogas technology
4. LITERATURE SURVEY
Biogas is produced by decomposition of biomass and animal wastes, human
excreta, sewage sludge and vegetable residues and poultry wastes by decomposer
organisms like bacteria under anaerobic (airless) condition. This process is
favoured by warm, wet and dark conditions. This involves chemical and
biological processes known as “anaerobic fermentation”, but “digestion” is
often used in anaerobic conditions, that lead to methane production.
Biogas consists of 70% methane [CH4] and 29% carbon dioxide [CO2],
and 1% of hydrogen sulphide [H2S], nitrogen [N2], and some hydrogen [H2]. It
has a calorific value of 20Mj/m3. Biogas is generated from the slurry [50% water
and 50% dung] at an average temperature of about 35OC by chemical waste and
biological process called anaerobic fermentation. The optimum temperature for
maximum production of biogas from slurry is about 37oC. The quantity of gas
production depends on the nature of dung used. The optimum temperature of
maximum production is achieved after a number of days, referred to as retention
period, after feeding the slurry into the digester of the system. The production of
gas starts only after the retention period. Supplying thermal energy to the system
by external means, i.e. by heating slurry using either passive or active method,
can reduce the length of the retention period.
The anaerobic digestion of organic material is a very complicated
biochemical process, involving hundreds of possible intermediate compounds and
reactions, each of which is catalyzed by specific enzymes or catalysts. However,
the overall chemical reaction is often simplified to:
Organic matter anaerobic CH4 + CO2 + H2 + NH3 +H2S…………(1)
Digestion
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In general, anaerobic digestion is considered to occur in the following stages:
The hydrolysis phase – liquefaction or polymer breakdown.
Acid formation phase
Methane formation.
In a biogas plant, all the three phases occur simultaneously and if only one
phase dominates, production of methane is seriously affected.
There are three main types of biogas plants suitable for integrated farms –
the fixed dome digester plant, the floating drum digester and the plastic covered
ditch. In this work, the fixed dome digester was used. Biogas has many
applications in integrated farms some of which are:
a). Biogas serves as a cooking fuel for farmers.
b). Biogas is used for lighting purposes on the farm.
c). Biogas lamps are use to warm birds and animals.
d). It is also possible to power an internal combustion (IC) engine that may
be found on the farms setting.
5. RESULTS AND DISCUSSIONS
5.1 Energy Audit and sizing of digester
The various forms of energy consumption per month and cost distribution account
were analyzed in this sub-section. The energy audit computed in table2 below is
based on fossil fuels used by the farms. From this table, Concordia farms utilize
1,218,111.25 Mj of fossil fuel per month (14,617,335 Mj per year) at a huge cost
of N1, 524,250.00 per month, (N18,291,000.00 per year).Table1 show heating
values of fuels used in the farm
Table 1: Heating vales of some fuels
Fuels Heating values (kj/kg) Heating values (Mj/kg)
Kerosene (paraffins) 46250 46.25Mj/kg
Fuel wood 12, 000 12 Mj/kg
Charcoal 9000 9 Mj/kg
Diesel (AGO) 46,000 46 Mj/kg
Motor petrol 46,800 46.8Mj/kg
[EASTop & McKonkey (1999)]
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Also, in order to design a digester of an appropriate and suitable capacity
of 681.3 M3 for the farm, the influent in (Kg) generated from livestock on the
farm were computed as seen in table3 and Fig.1 used in sizing the digester.
Table 3: Calculated Influent/day for Sizing the Farm Digester
Kinds Population Discharge per
day (kg)
TS value of
fresh
discharge
(% by wt)
Total influent
for each kinds
(Kg)
Cow 300 10 16 6000
Chicken 3,500 0.10 20 875
Pig 400 6 20 6000
Sheep 200 1.5 20 750
Total Influent generated on farm/day 13,625
With a hydraulic retention time (HRT) of 40 days, and Total influent (Q) of
13,625Kg, the digester volume was determined using the formulae
0.8V=Q HRT (1000Kg=1M3)……………………………………………(2)
From equation (1.2), the digester size is computed to be 681.3 M3
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Table 4: Biogas Energy Audit of the farm
Material Quantity (kg) Gas yield per
day (M3)
Total yield of biogas/
per day (M3)
Cattle dungs 3000 0.36 1,080
Sheep wastes 300 0.10 30
Pig droppings 2400 0.25 600
Poultry droppings 350 0.0112 3.92
Total volume of biogas yield per day 1,713.92
With 6,050kg of organic waste, 1,713.92 (M3) of biogas will be yielded
per day. This indicates that in one month, a total of 1,713.92 x 30 = 51,417.6 M3
of biogas will be generated in the farms. Since 1M3 of biogas is equivalent to
Fig.1: Calculated Dimensions of the cylindrical shaped biogas digester
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0.4kg of diesel, 0.6kg of petrol, 3.5kg of fuel wood, and 0.8kg of charcoal and
0.5kg of kerosene. One can say that generating 51,417.6M3 of biogas in a month
is equivalent to buying.
20,567.04kg of diesel/month = N1, 601,027.066 cost/month
30,850.56kg of petrol/ month = N2, 938,148.57
179,92.16kg of fuel wood/month = N1, 151,757.824
41,134.08kg of charcoal/ month = N102, 835.20
25,708.8kg of kerosene/ month = N2, 666,097.778
which is far more than the quantities Concordia farms purchase per month as
reflected in the energy analysis.
Also, a total of 51,417.6 m3 x 6,300 Kcal /m
3 = 323,930,880 kcal of
energy will be available to the farm in a month. 323,930,880 kcal = 3.2393088 x
1011
cal = 1.355909881 x 1012
joules = 1,355,909.881Mj of energy. This amount
of energy is far more than the calculated 1,218,111.25 Mj of energy consumed on
the farm per month.
So, the biogas generation prospects of the farm can actually meet the energy
needs of Concordia farms. This amount of energy can be utilize in cooking,
lightening, heating, warming etc. on the farm
5.2 Thermal analysis of the biogas plant
Result obtained from calculations reveal a thermal efficiency of 25 %.This
value shows poor efficiency of the heating system of the plant.It is obvious that
the various heat losses to the ambient and ground is responsible for the value
obtained.There is a significant decrease in thermal efficiency by the unglazing
effect due to reduced solar flux at the absorber of collector plate caused by
covection. The losses should be a minimum. The expression for thermal
efficiency is given below
)3......(..........)()(/)()/()exp(1
))(/)(
tITTCamUtFatNAat
tNAtITTCm
asossLc
csossst
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0 2 4 6 8 10 12 14 16 18 20 22 24 26 28 300
200
400
600
800
1000
1200
1400
1600
1800
2000
PTS [%]
Vb
[M3]
As seen in figure 2, the volume of biogas generated increases as percentage total
solid increase.In this research work,the total volume of biogas generated per day
stand at 1713.92 M3 and from the graph one can easily determine the average
PTS value to be 25.5 % .A marginal increase in PTS results in a geometrical
increase in the volume of biogas produced.
Figure 2: Graph of percentage total solid vs volume of biogas generated
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0 2000 4000 6000 8000 10000 12000 140000
100
200
300
400
500
600
700
Q [Kg]
Vd
[M3]
10 20 30 40 50 60 70 80 90 1000
200
400
600
800
1000
1200
1400
1600
1800
HRT [days]
Vd
[M3]
Figure 3 Graph of digester volume Vd vs substrate Q at HRT of 40 days
Figure 4: Variation of Vd with HRT at substrate value of 13,625 Kg
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As seen from result above, iron rod, iron wire and wood consume the highest
amount of construction cost of the digester plant representing 41.14%. Other
major costs are; sand & chippings, cement, and labour while digester accessories
gulp the list cost.
Cost payback time
Payback=capital cost/annual energy cost savings
Payback=5,954,100/18,214,175 = 0.33 years.
Energy payback time
Payback=1,218,111.25/1,355,909.88 = 0.9years
Figure 5: Cost Distribution of 681.3 m3 Biogas Plant
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5.3 Economic Valuation of Firewood and Charcoal
Use of firewood for cooking by a farm has negative effective on the
density of forest area in the locality, which in turn affects the microclimate of the
area and thus the society. Therefore, economic price of firewood has to be higher
for society than to an individual resulting into higher economic rate of returns on
the investment.
It is yet to be declared a single value for fuel wood that would reflect the
social cost or benefit of it. Some authorities have treated firewood as non-traded
goods and value it at lower than the financial price. Others value it at a percent
higher than the financial price. Still, other authorities have taken economic price
of firewood as 20 percent higher than the financial price.
5.4 Economic Valuation of Kerosene, p.m.s and Diesel
It is easier to arrive at the economic value of kerosene/PMS/Diesel as it is
readily marketed and the money value of subsidy in it can be calculated. In
Nigeria, petroleum products are refined locally and imported from oversees – for
imported goods; payment is made in US dollars. Assuming that the official
exchange rate between Nigeria’s Naira and the US dollars would fully reflect the
true economic value of goods traded with these currencies, the border price paid
by Nigeria is taken as the economic price of these products, while the cost of
production is the economic price when locally refined. About 10 percent is added
to this price to reflect the economic cost involved in transportation and handling
of kerosene/diesel/PMS within the country.
5.5 Economic Valuation of Labour
The use of biogas results in the saving of unskilled labour time. A wage
rate for unskilled labour has to be reduced by a factor that would reflect the cost
of large-scale farming. Gautam used a factor of 0.65 to arrive at the economic
wage rate of an unskilled labour (Gautam, 1988).
5.6 Valuation of Slurry
Slurry is valued for its content of soil nutrients, particularly N.P.K. As all
chemical fertilizers in Nigeria is imported, the economic values of N, P and K are
calculated at the international market price of N. P and K fertilizers.
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5.7 Investment Cost
The guarantee fee (if any) and service charge taken by biogas builders
should be deducted from the total investment, as they are only transfer of
payments. The subsidy (if any) should be included as part of the investment cost.
The total expenditure actually incurred for construction activities should be
reduced by a factor to reflect the true economic cost of materials and labor used in
construction. Gautam used the weighted average construction factor of 0.76 in the
case study referred above.
It is seen from the above that the economic cost of goods and services
used for biogas plant installation become lower than the costs used for financial
analysis. Also, the benefits of biogas use are valued at higher rate for economic
analysis than the financial analysis. Therefore, any plant that proves to be
financially viable to an individual user will still be viable at higher rate of return
from the economic or social point of view.
6.0 CONCLUSION
The choice of owning a biogas plant depends on; (1) the availability of
sufficient organic wastes which serves as raw material or input. (2) The energy
needs or requirements of the environment, it is to be installed. The volume of the
biogas plant will also depend on the amount of waste generated within the
locality and the amount of energy needed for consumption.
In the case study farm, we find out that the waste generation per day runs
into several thousands kilograms. This greatly influences the biogas digester
volume designed for these farms. Also, the amount of energy consumed per
month and resultantly per year runs from a million per day to several millions
mega joules per year.
In the thermal analysis, the instantaneous efficiency of the biogas plant
was used for the design of the active biogas system with a given heat capacity
(Ms Cs). From the economic point of view, the net cash flow of a 681.25m3 active
biogas plant without subsidy is positive in the first year. This indicates that
without subsidy, a user can still invest to get a positive return on investment. This
is not beyond the investment capacity for a commercial or large-scale or
mechanized farmer. Though there is still need for subsidy to encourage this
technology. Another factor notice in the economic feasibility is the higher benefit
of biogas plant use in terms of petrol, diesel and kerosene saved. This suggests
that the biogas plant may not be viewed as profitable if these savings is not used
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for generating more income by ploughing back these savings into the farming
business. Also, the biogas will be profitable if the labour saved is used for
generating income for the farm and the farm must attach values to all other
benefits of the biogas plant such as leisure, clean home stead/farm stead, and
better health.
Further more, the profitability of investment in biogas will increase with
the increase in the price of firewood, kerosene, diesel, etc. in the future.
So far, we have analyzed the organic waste generation of the case study
farms, its energy requirements, and we have compared its biogas generation
prospects with energy requirement. The economy studies also reveal the viability
of a project of installing an active biogas plant in Concordia farms Limited.
Biogas is a potential renewable energy source for rural Nigeria. Taking
biogas generation as a farm base activity, the energy requirements of these farms
can be meet.
From these analyses, I come to the conclusion that the designed biogas
plant will be suitable for this farm.
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