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Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of
Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com
Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223
1218 | P a g e
Experimental Investigation on Performance Improvement of Biogas Plant
Subbarao Chamarthi1
, N.Srinivasa Reddy 2
, G Ravi Chandra3
1
Department of Mechanical Engineering, Vardhaman college of engineering, India
2
Department of Mechanical Engineering, Vardhaman college of engineering, India
3
Department of Mechanical Engineering, Vardhaman college of engineering, India
ABSTRACT
Biogas is a sustainable fuel that stands
out from other biofuels because of the major
environmental and socio-economic benefits that
can be achieved. This opens up enormous
potential for sustainable economic growth and
will also improve our energy security.
An attempt has been made to find the
different ways to improve the overall
performance of biogas plant. The present work
comprise of improving the biogas yield in terms
of quality and quantity. Since it is a well known
fact that temperature improves the performance
of biogas plant, experimentation is carried out
to modify the existing mild steel dome based
biogas plant by transparent type fibre dome to
capture the green house effect.
Modifications are carried out in one of
the plant and the second plant is kept as a
reference. So far these two biogas plants were
studied for composition, yield, temperature
effect; pH value of the end digestate.
KEYWORDS: ENERGY SECURITY, TRANSPARENT
FIBRE DOME, MILD STEEL DOME, TEMPERATURE,
PH.
I. INTRODUCTION
Energy is the basis of human life. We
need energy to do work. Over the past few decades,
energy has been the subject of much debate.
Energy is the backbone of technology and
economic development. Our energy requirements
have spiraled over the years following the
industrial revolution. This rapid increase in our use
of energy has created problems of demand and
supply. The impending crisis the world over due to
overuse of non-renewable energy sources for
sustenance shall soon lead to a situation for all
concerned to take a prudent decision to start
depending on renewable energy sources for their
daily needs in order to conserve our finite natural
resources for generations to come.
After reading many studies and reports
about available technologies for treating wastes
mainly technologies treat organic wastes which
usually available for rural families especially
animals' dung, crops residues and domestic wastes
with centering on technologies that could be
constructed, operated and repaired by rural family
itself. It was found that many methods and
technologies could be applied to treat organic
wastes such as direct combustion, fermentation,
gasification, pyrolysis and anaerobic digestion.
Direct combustion means burning organic wastes
to get energy. It is a simple, easy and of low cost
process, but it generates smoke and ash which
means that this process associated with many
pollutant gases, polyaromatic hydrocarbons and
total suspended particles that cause chronic
diseases as asthma and lung cancer.
There is an increasing interest in producing biogas
from anaerobic digestion as a renewable source of
energy and as means of reducing our dependence
on fossil fuels. Anaerobic digestion can also be
useful in achieving several environmental benefits
and political objectives, such as more sustainable
strategies for waste management and agricultural
practices. The diversity is also reflected in the
varying effects (e.g. environmental impact) and
potential obstacles to the successful
implementation of biogas systems. A broad
systems perspective is therefore useful in order to
explore the benefits and drawbacks of different
biogas systems. So far, most of the research in this
field has focused on specific biogas systems or
parts of systems, for example, enhancing the
digestion technology or use of the biogas. There are
few comparative studies of biogas production that
include several alternatives for anaerobic digestion,
or studies that synthesize the current knowledge.
The overall objective of the work described in this
thesis was to assess biogas production from a
systems analytical perspective in order to enhance
the performance of a gobar gas based biogas plant.
In this case, “biogas production” should be
interpreted as the physical aspects of entire biogas
systems, from the raw materials digested to the
final use of the biogas and digestate produced. The
systems analytical approach considers primarily the
environmental impact of biogas production from a
life-cycle perspective, including energy
performance and emissions from the biogas
production systems. The first aim was to assess
when and under what conditions biogas and
anaerobic digestion are good alternatives from an
environmental point of view. The systems
analytical approach was then broadened in order to
identify factors of importance for the successful
Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of
Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com
Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223
1219 | P a g e
implementation of biogas production. . The second
aim was therefore to analyze the prospects for
successful performance of biogas plants.
Biogas technology has, therefore, the potential to
alleviate poverty providing substitutes for
expensive fuels and commercial fertilizers,
improving agric/aqua-cultural yields, reducing
local deforestation, creating jobs and income as
well as strengthening the indigenous technological
knowledge.
The report described here is motivated by
the need for better information concerning biogas
production from a broad systems perspective. The
principal audience envisaged is firstly those who
are interested in, or engaged in, biogas related
issues, including policy makers, decision makers,
researchers, consultants, farmers, and operators of
biogas plants, who require more information on the
environmental implications of biogas production.
Secondly, this Paper is directed towards those who
carry out life cycle assessment, and similar
analyses, of waste management, energy production,
agricultural practices, etc., and who require
information on the characteristics of biogas
production from a systems analytical perspective.
II. Experimental work:
2.1 Materials Used:
The materials used are
1. pH meter
2. Dry test gas meter
3. Digital thermometer
4. Stirrer.
The study was carried out on floating type mild
steel dome digester plant and a transparent dome
type plant with sizes of 2 m3
capacity at Vyara
which is located 60 km away from Surat on
operational parameters such as temperature , pH
and composition of methane yield for both the
plants.
2.2 Performance Monitoring of Test item and
Reference item
The two biogas digester types were fed
with 25kg cow-dung equal volumes of water and
thereafter a comparative study of the temperature
regimes inside them was undertaken for a period of
one month. And in assessing their performance, the
two biogas plants were used to kept for a retention
time of 10 days and during this time the
fermentation of the slurry takes place through
undergoing normal anaerobic digestion process
where thermopholic reactions takes place. During
this exercise, the biogas production and
temperature were monitored daily using a dry-test
gas meter and a digital thermometer respectively.
Figure 1: Determination of gas volume through dry gas meter
The results are noted daily for a period of 10 days and the readings are tabulated. The readings are noted
daily through digital dry gas meter to determine the biogas production rate.
Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of
Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com
Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223
1220 | P a g e
Table 1: Daily Biogas production rates at different slurry temperatures
Table shows the daily biogas yields from cow dung
on a daily basis under the various modes of
operation in both the digesters. The rates were
calculated as ratio of the amount of biogas
produced daily to the volume of the digester. The
average slurry temperatures for test item and
reference item are recorded as 31.71°c and 29.09°c
respectively. It is evident from the table that the
temperatures in the transparent type of digester
plants are having higher ratios than that of mild
steel dome type plant which shows a rise of 8.26 %
for the given specific period of time. This is
because of the fact that transparent dome type
digested plants can have higher absorption of heat
from the sun light .As a result of this the
temperature regimes inside the plant are higher .
From the rate of gas production shown in the table,
it is shown that as the concentration of slurry
increases during the days, the rate of production
also increase. The variation of rate of gas
production against time is clearly observed from
the graph.
Figure 2: Daily biogas production rate (cm3/day)
0
20
40
60
80
100
120
140
160
180
200
1 2 3 4 5 6 7 8 9 10
Biogasproductionrate
Numberof days
MSDD
TFDD
MILD STEEL DOME DIGESTSER TYPE TRANSPARENT DOME TYPE
DIGESTER
Duration
(days)
Biogas
produced
(cm3
/day)
slurry
temperature (°C)
Biogas
produced
(cm3
/day)
slurry
temperature (°C)
1 2.78 30.0 11.00 33.0
2 10.00 29.0 25.00 33.0
3 36.36 27.4 38.60 29.8
4 68.75 28.5 58.33 29.6
5 84.62 28.5 111.54 30.3
6 92.86 27.7 133.35 29.9
7 100.00 29.1 152.22 32.1
8 106.25 29.3 169.5 31.4
9 113.24 30.6 176.47 33.2
10 125.00 30.8 188.89 34.8
Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of
Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com
Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223
1221 | P a g e
From the graph it clearly shows that the biogas
production has increased enormously in the
transparent dome type as it is captures the solar
effect in which temperature regimes inside the
plant have been increased of better anaerobic
digestion process. Fluctuations in the temperatures
reduce the methane formation, because of
inhibition in growth of methanogens. In case of
better gas production the temperature regimes
should be maintained in the range between 30°c
and 40°c. From the results it concludes that
transparent type of dome is having greater
advantage compared to that of mild steel dome type
plant. In mild steel dome type plant the
temperatures are moderately maintained throughout
the day whereas is in transparent dome type
digester the temperatures are very much during the
sunlight as it captures much solar effect during the
day time .so finally the results reviewed that, the
digester temperatures in the transparent dome type
plant are higher than that of mild steel dome type
plant. The graph is plotted for the variation of
temperature during the number of days.
2.3 Determination of pH
The pH is measured daily with the help of
digital pH meter (BVM scientific). The pH meter
is used to determine the value of pH in the digested
slurry
The digesters of both the plants are monitored
using a digital pH meter and the pH values of both
the digesters are documented in order to analyze
the effect of pH with the temperature for a period
of ten days.
Table 2: Variation of pH with Temperature
From the table it clearly shows that, due to rise in
temperature of the digester the pH values are lower
as the anaerobic digestion process takes place
inside the digester for better formation of
methanogens. From the results it shows that the pH
values are maintained between 6.5 and 7.5 which
holds good for the digestion process and the pH
values of test item are slightly lower to that of
reference item. The temperature rise in digester
yields better digestion process for the process of
fermentation to take place as a result of which pH
is stabilized. 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 a value of 6.5 to 7.5.As anaerobic digestion
will occur best within in a pH range of 6.5 to 8.
The graph is plotted for the variation of pH with
the no. of days
MILD STEEL DOME DIGESTSER TYPE TRANSPARENT DOME TYPE
DIGESTER
Duration
(days) pH
slurry
temperature (°C) pH
slurry
temperature (°C)
1
6.5 30.0 6.2 33.0
2 6.9 29.0 6.6 33.0
3 6.4 27.4 6.5 29.8
4 7.2 28.5 6.8 29.6
5 6.9 28.5 6.8 30.3
6 7.2 27.7 6.9 29.9
7 7.2 29.1 7.0 32.1
8 6.8 29.3 6.8 31.4
9 7.3 30.6 6.9 33.2
10 7.0 30.8 6.8 34.8
Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of
Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com
Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223
1222 | P a g e
Figure 3: variation of pH with no. of days
From the graph, it clearly shows that the pH is
lower than the transparent fibre dome digester
compared to that of mild steel dome digester .This
is because higher concentration of acids are
produced during digestion process in transparent
dome digesters because of more temperature
regimes maintained inside the digester. The amount
of acids may exceed the potential buffer capacity
due to better formation of methanogens during the
digestion process. So finally it suggested that the
pH in the transparent dome digesters are
comparatively lower than that of mild steel dome
digester because of higher temperature regimes
maintained inside the digester.
III. Conclusion
The experimental and the field results from this
study and the experience gained from the operation
of biogas production system lead to the following
conclusions:
 The use of transparent fibre dome digester
reduced the digester thermal losses and a
positive rise in the temperature regimes inside
the digester plant which leads for better
anaerobic digestion for the formation of
methanogens.
 The use of transparent fibre dome digester
keeps the dome completely more airtight than
the conventional plants with less compatibility
and well structured which lead to better
methane yields.
 An increased temperature facilitates faster
reaction rates and hence faster gas yields.
Operation at higher temperatures yields greater
sterilization of the end digestate.
In the present study, the testing of transparent
fibre dome as an alternate building material for
biogas plant proves to be more effective than
conventional biogas plant which is evident from the
experimental results. The study mainly focuses on
increase in temperature regimes of the biogas plant
for the better anaerobic digestion process. The
temperature plays a crucial role in fermentation of
the slurry for the better formation of
methanogens.An increased temperature in the
digester tank facilitates faster reaction rates and
hence faster gas yields are produced. The results
reviewed that the temperature regimes are
maintained moderately higher than that of mild
steel dome digester which yields greater
sterilization of the end digestate and faster gas
yields.
Finally it concluded that the usage of
transparent fibre dome type digester proves to be
more effective than that of conventional mild steel
dome digester in terms of performance and
economical viability is considered.
REFERENCES
[1] Khapre UL. Studies on biogas utilization
for domestic cooking. Paper presented at
XXV annual convention of ISAE, held at
CTAE, Udaipur; 1989.
[2] Janani Chakravarthi “Biogas and energy
production from cattle waste” IEEE
Energy Conversion Engineering
Conference, IECEC-97 32nd Intersociety
pp: 648 - 651 vol.1.1997.
[3] Karve of Pune A.D (2006). Compact
biogas plant compact low-cost digester
from Waste starch.
www.bioenergylists.org.
[4] The University of Southampton and
Greenfinch Ltd. - Biodigestion of kitchen
waste a comparative evaluation of
5.6
5.8
6
6.2
6.4
6.6
6.8
7
7.2
7.4
1 2 3 4 5 6 7 8 9 10
pH
Numberof days
MSDD
TFDD
Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of
Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com
Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223
1223 | P a g e
mesophilic and thermophilic biodigestion
for the Stabilization and sanitization of
kitchen waste.
[5] http://www.renewableenergyworld.com
[6] www.fao.org
Author 1: Subbarao Chamarthi
Short Biography
Subbarao chamarthi, born in 1987 in
Andhrapradesh, India, received his B.Tech. Degree
in 2009 from the Department of Mechanical
Engineering, Koneru Lakshmiah University; and
his M.Tech. in 2011 from Sardar Vallababhai Patel
National Institute of Technology. Thereafter he
worked as a process engineer in GRP Pipes
industry for a period of six months. Then he had
worked as an Assistant professor in the Department
of Mechanical Engineering in Smt.S.R.Patel
Engineering College, Gujarat for a period of 1 year
2 months. Now presently he is working as Assistant
Professor in the Department of Mechanical
Engineering in Vardhaman College of Engineering.
Author 2:N.Srinivasa Reddy
Short Biography
Mr.N.Srinivasa Reddy, born in 1972 in
Andhrapradesh, India, received his B.Tech. Degree
in 1994 from the Department of Mechanical
Engineering, SRKR Bhimavaram, Andhrapradesh;
and his M.Tech. in 2001 from JNTU-
Hyderabad.Thereafter he worked as a Assistant
professor for several years. Now presently he is
working as a HOD in the Department of
Mechanical Engineering in Vardhaman College of
Engineering.
Author 3: G Ravi Chandra
Short Biography
Mr.G Ravi Chandra, born in 1983 in
Andhrapradesh, India, received his B.Tech. Degree
in 2005 from the Department of Mechanical
Engineering, MVGR College of Engineering,
Andhrapradesh; and his M.Tech. in 2009 from
SRKR Bhimavaram, Andhrapradesh . Now
Presently he is working as Assistant Professor in
the Department of Mechanical Engineering in
Vardhaman College of Engineering.

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Gx3312181223

  • 1. Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223 1218 | P a g e Experimental Investigation on Performance Improvement of Biogas Plant Subbarao Chamarthi1 , N.Srinivasa Reddy 2 , G Ravi Chandra3 1 Department of Mechanical Engineering, Vardhaman college of engineering, India 2 Department of Mechanical Engineering, Vardhaman college of engineering, India 3 Department of Mechanical Engineering, Vardhaman college of engineering, India ABSTRACT Biogas is a sustainable fuel that stands out from other biofuels because of the major environmental and socio-economic benefits that can be achieved. This opens up enormous potential for sustainable economic growth and will also improve our energy security. An attempt has been made to find the different ways to improve the overall performance of biogas plant. The present work comprise of improving the biogas yield in terms of quality and quantity. Since it is a well known fact that temperature improves the performance of biogas plant, experimentation is carried out to modify the existing mild steel dome based biogas plant by transparent type fibre dome to capture the green house effect. Modifications are carried out in one of the plant and the second plant is kept as a reference. So far these two biogas plants were studied for composition, yield, temperature effect; pH value of the end digestate. KEYWORDS: ENERGY SECURITY, TRANSPARENT FIBRE DOME, MILD STEEL DOME, TEMPERATURE, PH. I. INTRODUCTION Energy is the basis of human life. We need energy to do work. Over the past few decades, energy has been the subject of much debate. Energy is the backbone of technology and economic development. Our energy requirements have spiraled over the years following the industrial revolution. This rapid increase in our use of energy has created problems of demand and supply. The impending crisis the world over due to overuse of non-renewable energy sources for sustenance shall soon lead to a situation for all concerned to take a prudent decision to start depending on renewable energy sources for their daily needs in order to conserve our finite natural resources for generations to come. After reading many studies and reports about available technologies for treating wastes mainly technologies treat organic wastes which usually available for rural families especially animals' dung, crops residues and domestic wastes with centering on technologies that could be constructed, operated and repaired by rural family itself. It was found that many methods and technologies could be applied to treat organic wastes such as direct combustion, fermentation, gasification, pyrolysis and anaerobic digestion. Direct combustion means burning organic wastes to get energy. It is a simple, easy and of low cost process, but it generates smoke and ash which means that this process associated with many pollutant gases, polyaromatic hydrocarbons and total suspended particles that cause chronic diseases as asthma and lung cancer. There is an increasing interest in producing biogas from anaerobic digestion as a renewable source of energy and as means of reducing our dependence on fossil fuels. Anaerobic digestion can also be useful in achieving several environmental benefits and political objectives, such as more sustainable strategies for waste management and agricultural practices. The diversity is also reflected in the varying effects (e.g. environmental impact) and potential obstacles to the successful implementation of biogas systems. A broad systems perspective is therefore useful in order to explore the benefits and drawbacks of different biogas systems. So far, most of the research in this field has focused on specific biogas systems or parts of systems, for example, enhancing the digestion technology or use of the biogas. There are few comparative studies of biogas production that include several alternatives for anaerobic digestion, or studies that synthesize the current knowledge. The overall objective of the work described in this thesis was to assess biogas production from a systems analytical perspective in order to enhance the performance of a gobar gas based biogas plant. In this case, “biogas production” should be interpreted as the physical aspects of entire biogas systems, from the raw materials digested to the final use of the biogas and digestate produced. The systems analytical approach considers primarily the environmental impact of biogas production from a life-cycle perspective, including energy performance and emissions from the biogas production systems. The first aim was to assess when and under what conditions biogas and anaerobic digestion are good alternatives from an environmental point of view. The systems analytical approach was then broadened in order to identify factors of importance for the successful
  • 2. Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223 1219 | P a g e implementation of biogas production. . The second aim was therefore to analyze the prospects for successful performance of biogas plants. Biogas technology has, therefore, the potential to alleviate poverty providing substitutes for expensive fuels and commercial fertilizers, improving agric/aqua-cultural yields, reducing local deforestation, creating jobs and income as well as strengthening the indigenous technological knowledge. The report described here is motivated by the need for better information concerning biogas production from a broad systems perspective. The principal audience envisaged is firstly those who are interested in, or engaged in, biogas related issues, including policy makers, decision makers, researchers, consultants, farmers, and operators of biogas plants, who require more information on the environmental implications of biogas production. Secondly, this Paper is directed towards those who carry out life cycle assessment, and similar analyses, of waste management, energy production, agricultural practices, etc., and who require information on the characteristics of biogas production from a systems analytical perspective. II. Experimental work: 2.1 Materials Used: The materials used are 1. pH meter 2. Dry test gas meter 3. Digital thermometer 4. Stirrer. The study was carried out on floating type mild steel dome digester plant and a transparent dome type plant with sizes of 2 m3 capacity at Vyara which is located 60 km away from Surat on operational parameters such as temperature , pH and composition of methane yield for both the plants. 2.2 Performance Monitoring of Test item and Reference item The two biogas digester types were fed with 25kg cow-dung equal volumes of water and thereafter a comparative study of the temperature regimes inside them was undertaken for a period of one month. And in assessing their performance, the two biogas plants were used to kept for a retention time of 10 days and during this time the fermentation of the slurry takes place through undergoing normal anaerobic digestion process where thermopholic reactions takes place. During this exercise, the biogas production and temperature were monitored daily using a dry-test gas meter and a digital thermometer respectively. Figure 1: Determination of gas volume through dry gas meter The results are noted daily for a period of 10 days and the readings are tabulated. The readings are noted daily through digital dry gas meter to determine the biogas production rate.
  • 3. Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223 1220 | P a g e Table 1: Daily Biogas production rates at different slurry temperatures Table shows the daily biogas yields from cow dung on a daily basis under the various modes of operation in both the digesters. The rates were calculated as ratio of the amount of biogas produced daily to the volume of the digester. The average slurry temperatures for test item and reference item are recorded as 31.71°c and 29.09°c respectively. It is evident from the table that the temperatures in the transparent type of digester plants are having higher ratios than that of mild steel dome type plant which shows a rise of 8.26 % for the given specific period of time. This is because of the fact that transparent dome type digested plants can have higher absorption of heat from the sun light .As a result of this the temperature regimes inside the plant are higher . From the rate of gas production shown in the table, it is shown that as the concentration of slurry increases during the days, the rate of production also increase. The variation of rate of gas production against time is clearly observed from the graph. Figure 2: Daily biogas production rate (cm3/day) 0 20 40 60 80 100 120 140 160 180 200 1 2 3 4 5 6 7 8 9 10 Biogasproductionrate Numberof days MSDD TFDD MILD STEEL DOME DIGESTSER TYPE TRANSPARENT DOME TYPE DIGESTER Duration (days) Biogas produced (cm3 /day) slurry temperature (°C) Biogas produced (cm3 /day) slurry temperature (°C) 1 2.78 30.0 11.00 33.0 2 10.00 29.0 25.00 33.0 3 36.36 27.4 38.60 29.8 4 68.75 28.5 58.33 29.6 5 84.62 28.5 111.54 30.3 6 92.86 27.7 133.35 29.9 7 100.00 29.1 152.22 32.1 8 106.25 29.3 169.5 31.4 9 113.24 30.6 176.47 33.2 10 125.00 30.8 188.89 34.8
  • 4. Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223 1221 | P a g e From the graph it clearly shows that the biogas production has increased enormously in the transparent dome type as it is captures the solar effect in which temperature regimes inside the plant have been increased of better anaerobic digestion process. Fluctuations in the temperatures reduce the methane formation, because of inhibition in growth of methanogens. In case of better gas production the temperature regimes should be maintained in the range between 30°c and 40°c. From the results it concludes that transparent type of dome is having greater advantage compared to that of mild steel dome type plant. In mild steel dome type plant the temperatures are moderately maintained throughout the day whereas is in transparent dome type digester the temperatures are very much during the sunlight as it captures much solar effect during the day time .so finally the results reviewed that, the digester temperatures in the transparent dome type plant are higher than that of mild steel dome type plant. The graph is plotted for the variation of temperature during the number of days. 2.3 Determination of pH The pH is measured daily with the help of digital pH meter (BVM scientific). The pH meter is used to determine the value of pH in the digested slurry The digesters of both the plants are monitored using a digital pH meter and the pH values of both the digesters are documented in order to analyze the effect of pH with the temperature for a period of ten days. Table 2: Variation of pH with Temperature From the table it clearly shows that, due to rise in temperature of the digester the pH values are lower as the anaerobic digestion process takes place inside the digester for better formation of methanogens. From the results it shows that the pH values are maintained between 6.5 and 7.5 which holds good for the digestion process and the pH values of test item are slightly lower to that of reference item. The temperature rise in digester yields better digestion process for the process of fermentation to take place as a result of which pH is stabilized. 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 a value of 6.5 to 7.5.As anaerobic digestion will occur best within in a pH range of 6.5 to 8. The graph is plotted for the variation of pH with the no. of days MILD STEEL DOME DIGESTSER TYPE TRANSPARENT DOME TYPE DIGESTER Duration (days) pH slurry temperature (°C) pH slurry temperature (°C) 1 6.5 30.0 6.2 33.0 2 6.9 29.0 6.6 33.0 3 6.4 27.4 6.5 29.8 4 7.2 28.5 6.8 29.6 5 6.9 28.5 6.8 30.3 6 7.2 27.7 6.9 29.9 7 7.2 29.1 7.0 32.1 8 6.8 29.3 6.8 31.4 9 7.3 30.6 6.9 33.2 10 7.0 30.8 6.8 34.8
  • 5. Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223 1222 | P a g e Figure 3: variation of pH with no. of days From the graph, it clearly shows that the pH is lower than the transparent fibre dome digester compared to that of mild steel dome digester .This is because higher concentration of acids are produced during digestion process in transparent dome digesters because of more temperature regimes maintained inside the digester. The amount of acids may exceed the potential buffer capacity due to better formation of methanogens during the digestion process. So finally it suggested that the pH in the transparent dome digesters are comparatively lower than that of mild steel dome digester because of higher temperature regimes maintained inside the digester. III. Conclusion The experimental and the field results from this study and the experience gained from the operation of biogas production system lead to the following conclusions:  The use of transparent fibre dome digester reduced the digester thermal losses and a positive rise in the temperature regimes inside the digester plant which leads for better anaerobic digestion for the formation of methanogens.  The use of transparent fibre dome digester keeps the dome completely more airtight than the conventional plants with less compatibility and well structured which lead to better methane yields.  An increased temperature facilitates faster reaction rates and hence faster gas yields. Operation at higher temperatures yields greater sterilization of the end digestate. In the present study, the testing of transparent fibre dome as an alternate building material for biogas plant proves to be more effective than conventional biogas plant which is evident from the experimental results. The study mainly focuses on increase in temperature regimes of the biogas plant for the better anaerobic digestion process. The temperature plays a crucial role in fermentation of the slurry for the better formation of methanogens.An increased temperature in the digester tank facilitates faster reaction rates and hence faster gas yields are produced. The results reviewed that the temperature regimes are maintained moderately higher than that of mild steel dome digester which yields greater sterilization of the end digestate and faster gas yields. Finally it concluded that the usage of transparent fibre dome type digester proves to be more effective than that of conventional mild steel dome digester in terms of performance and economical viability is considered. REFERENCES [1] Khapre UL. Studies on biogas utilization for domestic cooking. Paper presented at XXV annual convention of ISAE, held at CTAE, Udaipur; 1989. [2] Janani Chakravarthi “Biogas and energy production from cattle waste” IEEE Energy Conversion Engineering Conference, IECEC-97 32nd Intersociety pp: 648 - 651 vol.1.1997. [3] Karve of Pune A.D (2006). Compact biogas plant compact low-cost digester from Waste starch. www.bioenergylists.org. [4] The University of Southampton and Greenfinch Ltd. - Biodigestion of kitchen waste a comparative evaluation of 5.6 5.8 6 6.2 6.4 6.6 6.8 7 7.2 7.4 1 2 3 4 5 6 7 8 9 10 pH Numberof days MSDD TFDD
  • 6. Subbarao Chamarthi, N.Srinivasa Reddy, G Ravi Chandra / International Journal of Engineering Research and Applications (IJERA) ISSN: 2248-9622 www.ijera.com Vol. 3, Issue 3, May-Jun 2013, pp.1218-1223 1223 | P a g e mesophilic and thermophilic biodigestion for the Stabilization and sanitization of kitchen waste. [5] http://www.renewableenergyworld.com [6] www.fao.org Author 1: Subbarao Chamarthi Short Biography Subbarao chamarthi, born in 1987 in Andhrapradesh, India, received his B.Tech. Degree in 2009 from the Department of Mechanical Engineering, Koneru Lakshmiah University; and his M.Tech. in 2011 from Sardar Vallababhai Patel National Institute of Technology. Thereafter he worked as a process engineer in GRP Pipes industry for a period of six months. Then he had worked as an Assistant professor in the Department of Mechanical Engineering in Smt.S.R.Patel Engineering College, Gujarat for a period of 1 year 2 months. Now presently he is working as Assistant Professor in the Department of Mechanical Engineering in Vardhaman College of Engineering. Author 2:N.Srinivasa Reddy Short Biography Mr.N.Srinivasa Reddy, born in 1972 in Andhrapradesh, India, received his B.Tech. Degree in 1994 from the Department of Mechanical Engineering, SRKR Bhimavaram, Andhrapradesh; and his M.Tech. in 2001 from JNTU- Hyderabad.Thereafter he worked as a Assistant professor for several years. Now presently he is working as a HOD in the Department of Mechanical Engineering in Vardhaman College of Engineering. Author 3: G Ravi Chandra Short Biography Mr.G Ravi Chandra, born in 1983 in Andhrapradesh, India, received his B.Tech. Degree in 2005 from the Department of Mechanical Engineering, MVGR College of Engineering, Andhrapradesh; and his M.Tech. in 2009 from SRKR Bhimavaram, Andhrapradesh . Now Presently he is working as Assistant Professor in the Department of Mechanical Engineering in Vardhaman College of Engineering.