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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1755
ACTIVITY OF DIFFERENT INNOCULATION ON FOOD WASTE ANAEROBIC
DIGESTION SYSTEM OF BIT SINDRI
1Sandeep Kumar,2Prof. Sunil Kumar
Mechanical Engineering ,BIT Sindri, Dhanbad.
------------------------------------------------------------***-----------------------------------------------------------------------
ABSTRACT:
The present research work focuses on the biogas
production from kitchen waste generated at the
BIT Sindri campus and to investigate the effects
of the key process parameters like pH and
temperature, by operating a pilot scale setup in
two stage thermophilic and mesophilic digestion
conditions. In experimental setup, a comparison
of the digestion of food wastes in small scale was
done. In this experiment three setups were
operated in mesophilic, thermophilic and two
stage mesophilic and thermophilic conditions
respectively.
In batch condition, maximum of 7.45 Liters
biogas was produced from the digestion of 6 kg
of food wastes in 25 days. The initial total solid
content of the waste slurry was
measured to be 10.27% which was reduced to
5.51% on 25th day. The initial total carbohydrate
and volatile fatty acid concentration was 61.2
g/L and 2475.5 mg/L
respectively. After 24 days of digestion, the total
carbohydrate concentration was decreased to
22.3 g/L, whereas volatile fatty acid
concentration was increased to 4954 mg/L. The
project work signifies that the kitchen waste can
be used as a potential source for biogas
production using two stage
digestion process and thus effective waste
management can be achieved.
Electronic waste is informally known as e-waste
for the electronic products nearing the end of
their useful life. The e- waste products contain
materials that are hazardous to the human
beings, depending on their condition & density.
The hazardous content of these materials pose a
threat to human health and environment. In
India electronic waste is producing in a huge
quantity , since it has emerged as an it giant and
due to modernization of lifestyle. Fridge, cell
phones, discarded computers, mobiles &
batteries etc, if not disposed properly, can leach
lead & other substances to soil & underground
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1756
water. This paper highlights the issues related to
e-waste disposal methods & management of e-
waste
Keywords: mesophilic, thermophilic,
anaerobic, disposal methods, sources.
1.INTRODUCTION:
Anaerobic digestion is generally used, proven
processes that is being used for the treatment of
the solid wastes. Anaerobic digestion is a process
in which the biological processes like
biodigestion by the microbes occur. Anaerobic
digestion processes breakdown the organic
matter in the feed materials in anaerobic
conditions i.e., in the absence of oxygen. These
processes stabilizes these waste materials
against rapid decomposition. The conversion
process is conservative in nature which
produces a stable digestive that can be used as a
bio-fertilizer. The methane gas and carbon
dioxide are also produced which are together
known as biogas. Thus in addition to treatment
of the solid wastes, anaerobic digestion also
allows recovery of energy value by conversion of
the volatile solids into biogas. The process also
functions as a waste material disposal system.
Food wastes have become a major source of
substrate for the biogas plants due to their high
organic content. Food wastes has also been used
as substrate in combination with animal dung in
biogas plants to obtain an overall high
production of biogas.
Also electronic wastes also increased in daily life.
Consumer electronics have become an integral
part of daily life and revolutionized the way we
communicate, retrieve information, and view
entertainment. Between computers, televisions,
mobile devices, electronic games, and even
devices which measure metabolic rate.
Electronic industry is the world’s largest and
Innovative industry for its kind. Every year tons
of electronic items are shipped over oceans,
however, after their usage time they are become
a complex waste matter which consists of many
hazardous heavy metals, acids, toxic chemicals
and non degradable plastics. Many are dumped,
burnt or exported to recyclers. The Biogas
produced by anaerobic digestion process has
methane as its major constituent.
2.EXPERIMENTAL SETUP (Small Scale):
Three different digesters were setup under
different conditions with same initial
composition were installed as below. The food
waste used for the study in this project was
collected from the mess at BIT Sindri. The food
waste samples collected consisted of mixed
wastes i.e., cooked wastes, uncooked wastes. The
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1757
indigestible wastes like onion peels, small twigs,
egg shells, etc. were removed from the collected
food wastes manually. Now electronic waste
collected from BIT, Sindri campus.
Sources of Electronic Waste in India
The main sources of electronic waste in India
are:
A. Solder in printed circuit, glass panels &
gaskets in Computer monitor
B. Chip resistors & Semiconductors
C. Refrigerators & Batteries
D. Mobiles
E. Microwave & Air Conditioners etc.
Disposal Methods
The toxic materials, which are used in
manufacturing of Electronic good can damage to
the environment. It contains Cathode ray tubes
(crts), printed board assemblies, Capacitors,
mercury switches and relays, batteries, liquid
Crystal displays(lcds), cartridges from
photocopying machines, selenium drums
(photocopier) and electrolytes. The Disposal
methods are as follows.
Land filling- this method is suitable for
quantitatively small e-waste i.e. domestic & small
users. E -Waste is piled up & covered with other
domestic waste & soil.
Incineration- e-waste is burnt in controlled
environment. The Toxic gases or smoke is
released into atmosphere.
Reuse-the spares &components are removed
from the device & with some modification, they
are used for other applications.
Recycle-the important ingredients of e-waste is
collected & sent to manufacturing companies
producing similar components.
The food wastes was then weighed 400gm for
each setup. The food waste was crushed using a
mixer grinder along with diluting it to 1 liter
with water to form homogenized slurry(the food
waste was diluted at a rate of 1:1.5 with water).
The initial analysis of the food wastes before it
was put into the reactor were performed, the
same day it was collected from the hall. The
analysis was done as follows.
 The diluted food wastes collected on the
1st day were analyzed for Total Solids
(TS), Volatile Solids (VS), Total
Carbohydrates (TC) and pH.
 The TS-VS content for each of the
digester setup was measured every 5
days from the start of the setup.
 The total Carbohydrate content for each
of the digester setup was measured using
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1758
Phenol-Sulfuric acid method every 3 days
from the start of the setup.
 pH was measured every 2 days and was
adjusted by adding sodium hydroxide to
regulate the pH around 7.
 Gas production of each setup was
measured every day.
 The substrate in the setup was kept well
mixed by shaking the setup 4-5 times a
day.
 Hot water bath was used for heating and
maintaining temperature during
thermophilic stage.
Materials Used for the setup:
 3 separate 1.2 liter plastic bottles.
 400 gm grinded kitchen waste diluted to
1 liter with water for each setup.
 100ml diluted cow dung slurry was added
and used as inoculums.
 Rest space was left empty.
Setup: 1. 400gm food waste diluted with water
to make 1litre then 100ml diluted cow dung
slurry was kept under mesophilic conditions at
room temperature. pH of the setup was
measured and adjusted to 6.6 initially. This
setup was operated only for 20 days.
Setup: 2. 400gm food waste diluted with water
to make 1litre then 100ml diluted cow dung
slurry. This setup was initially kept at
thermophilic temperature (around 55° C) in a
water bath for 2days and then under mesophilic
conditions at room temperature and 50 ml more
inoculums was added. pH of the setup was
measured and adjusted to 6.7initially. This
setup was operated only for 20 days.
Setup: 3. 400gm food waste diluted with water
to make 1litre then 100ml diluted cow dung
slurry was kept under thermophilic temperature
(around 55° C) in a water bath. pH of the setup
was measured and adjusted to 6.5 initially. This
setup was operated only for 10 days.
3.EXPERIMENTAL SETUP (Pilot Scale):
The pilot scale biogas plant was made from the
following components:-
A. Inlet tank - From this tank the crushed food
waste material was to be added. This part was
made from a plastic bucket in which the slurry
was prepared then added to the pre-digestion
tank through the inlet of that pre-digester tank.
Material used – Plastic Bucket (1 Nos.)
B. Pre-digester tank - here the waste materials
were heated around temperature of 50-60°C so
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1759
that thermophilic hydrolytic bacteria would
grow. The substrate remained in this tank for 2
days. The heating helps in the faster digestion of
the food waste.
Material used – Steel Cylindrical Tank (10 Liters
capacity, 1 Nos.)
C. Main digestion tank – The waste materials
after getting digested in the pre digester tanks
for a 2 days was passed onto the main digester
tank where the mesophilic methanogenic
bacteria was allowed to grow with the addition
of some new inoculums, which digest the food
wastes further to produce methane gas.
Material used – Steel Cylindrical Tank (20 Liters
capacity, 1 Nos.)
D. Gas collection unit – This unit was used to collect
the gas that was generated from the digestion of the
food wastes in the digester tanks. The gas was
collected over water and was characterized to find
the type of gas produced.
Material used – Plastic bottles (2 Liters
capacity, 2 Nos.)
E. Slurry collection unit – This unit was be used
to collect the digested slurry of the food wastes
at regular intervals for the analysis. This slurry
was be analyzed to study their characteristics.
Material required – Plastic beakers (1 Nos.)
Other Materials required – PVC pipes, silicon
pipes and valves was be used to connect
different units of the plant.
Gas Production
Table: Gas Production of the pilot scale
setups with time
Day Gas
Production
Day Gas
Production
1 7200 14 7100
2 7050 15 7400
3 4850 16 7150
4 5000 17 7250
5 4800 18 7450
6 5540 19 7300
7 5750 20 7450
8 6200 21 7350
9 6250 22 7200
10 6350 23 7300
11 6150 24 7200
12 6850 25 7450
13 7150
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1760
4.Gas Analysis:
Table: Gas analysis of the pilot scale setup
with time
Day H2(%) CO2(%) CH4(%) CO(%) O2(%)
5 3.11 66.2 0 0.01 6.22
10 0 70 1.2 0.01 8
18 0 56.12 10.2 0.01 8.21
25 0 45.3 18.56 0.01 6.41
5.CONCLUSION:
The pilot scale plant was based on two stage
thermophilic and mesophilic digestion process
and operated as a batch reactor under controlled
conditions of pH and temperature. A constant
rate of gas production was achieved but
accumulation of volatile fatty acids was also
observed. In batch condition, it was observed
that a maximum of 7.45 Liters biogas was
produced from the digestion of 6 kg of food
wastes in 25 days. Initially the total solids of the
waste slurry was measured to be 10.27% on the
day of starting the reactor and 5.51% on 25th
day. The total carbohydrates degradation was
measured to be 61.2 g/L on the day of starting
the reactor and 22.3 g/L on 24th day. The
volatile fatty acid concentration was measured
as 2475.5 mg/L on the day of starting the reactor
and 4954 mg/L on 24th day.
The future prospect of the project can be the
improvement of biogas production from kitchen
wastes by incorporating additives and
optimization of other process parameters in the
two stage anaerobic digestion process.
It is confirmed that the public awareness and co-
operation of manufactures are essential for the
advancement of e-waste management system.
0
10
20
30
40
50
60
70
80
5 10 18 25
Gas(%)
Days
Gas Analysis
H2(%)
CO2(%)
CH4(%)
CO(%)
O2(%)
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1761
Also e-wastes are the known major source of
heavy metals, hazardous chemicals and
carcinogens, certainly diseases related to skin,
respiratory, intestinal, immune, and endocrine
and nervous systems including cancers can be
prevented by proper management and disposal
of e-waste.
6.ACKNOWLEDGEMENT:
I acknowledge Prof. Sunil Kumar, Mechanical
Engineering department, BIT Sindri, Dhanbad for
supporting me during completion of entire
project.
7.REFERENCE:
1. Chanakya, H. and S. Malayil, Anaerobic digestion
for bio-energy from agro-residues and other solid
wastes—an overview of science, technology and
sustainability. Journal of the Indian Institute of
Science, 2012.92(1): p. 111-144.
2. Palaniswamy, D., et al. Experimental investigation
of biogas production from food waste and analysis
for the waste energy recovery and utilization from
institutions of state of Tamil Nadu in India. in
Intelligent Systems and Control (ISCO), 2013 7th
International Conference on. 2013. IEEE.
3. Kale, S. and S. Mehetre, Kitchen waste based biogas
plant. Nuclear Agriculture and Biotechnology
Division, Bhabha Atomic Research Centre, India,
2006.
4. Fulekar, M., Environmental biotechnology. 2010:
Science Publishers.
5. Salunkhe, D., R. Rai, and R. Borkar, BIOGAS
TECHNOLOGY. International Journal of Engineering
Science & Technology, 2012.4(12).
6.Vindis, P., et al., The impact of mesophilic and
thermophilic anaerobic digestion on biogas
production. Journal of achievements in materials and
manufacturing Engineering, 2009.36(2): p. 192-198.
49
7.ATSDR (2007b) (cited in Kevin et al., 2008) (cited
in Kevin et al., 2008) Toxicological Profile for lead.
United States Public Health Service, Agency for Toxic
Substances and Disease Registry, August 2007.
8. Basel Action uploaded on (2013) Exporting Harm:
The High-Tech Trashing of Asia [video file] Retrieved
fromhttp://www.youtube.com/watch?v=yDSWGV3j
Gek
9. Lakshmi Raghupathy et.al, e-waste recycling in
India –bridging the gap between the informal and
formal sector.
10. Northeast Recycling Council (NERC). “Recycling
Economic Information Study Update:
Delaware, Maine, Massachusetts, New York, and
Pennsylvania.” February 2009. Web. 6 June 2012.

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Activity of different innoculation on food waste anaerobic digestion system of bit sindri

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1755 ACTIVITY OF DIFFERENT INNOCULATION ON FOOD WASTE ANAEROBIC DIGESTION SYSTEM OF BIT SINDRI 1Sandeep Kumar,2Prof. Sunil Kumar Mechanical Engineering ,BIT Sindri, Dhanbad. ------------------------------------------------------------***----------------------------------------------------------------------- ABSTRACT: The present research work focuses on the biogas production from kitchen waste generated at the BIT Sindri campus and to investigate the effects of the key process parameters like pH and temperature, by operating a pilot scale setup in two stage thermophilic and mesophilic digestion conditions. In experimental setup, a comparison of the digestion of food wastes in small scale was done. In this experiment three setups were operated in mesophilic, thermophilic and two stage mesophilic and thermophilic conditions respectively. In batch condition, maximum of 7.45 Liters biogas was produced from the digestion of 6 kg of food wastes in 25 days. The initial total solid content of the waste slurry was measured to be 10.27% which was reduced to 5.51% on 25th day. The initial total carbohydrate and volatile fatty acid concentration was 61.2 g/L and 2475.5 mg/L respectively. After 24 days of digestion, the total carbohydrate concentration was decreased to 22.3 g/L, whereas volatile fatty acid concentration was increased to 4954 mg/L. The project work signifies that the kitchen waste can be used as a potential source for biogas production using two stage digestion process and thus effective waste management can be achieved. Electronic waste is informally known as e-waste for the electronic products nearing the end of their useful life. The e- waste products contain materials that are hazardous to the human beings, depending on their condition & density. The hazardous content of these materials pose a threat to human health and environment. In India electronic waste is producing in a huge quantity , since it has emerged as an it giant and due to modernization of lifestyle. Fridge, cell phones, discarded computers, mobiles & batteries etc, if not disposed properly, can leach lead & other substances to soil & underground
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1756 water. This paper highlights the issues related to e-waste disposal methods & management of e- waste Keywords: mesophilic, thermophilic, anaerobic, disposal methods, sources. 1.INTRODUCTION: Anaerobic digestion is generally used, proven processes that is being used for the treatment of the solid wastes. Anaerobic digestion is a process in which the biological processes like biodigestion by the microbes occur. Anaerobic digestion processes breakdown the organic matter in the feed materials in anaerobic conditions i.e., in the absence of oxygen. These processes stabilizes these waste materials against rapid decomposition. The conversion process is conservative in nature which produces a stable digestive that can be used as a bio-fertilizer. The methane gas and carbon dioxide are also produced which are together known as biogas. Thus in addition to treatment of the solid wastes, anaerobic digestion also allows recovery of energy value by conversion of the volatile solids into biogas. The process also functions as a waste material disposal system. Food wastes have become a major source of substrate for the biogas plants due to their high organic content. Food wastes has also been used as substrate in combination with animal dung in biogas plants to obtain an overall high production of biogas. Also electronic wastes also increased in daily life. Consumer electronics have become an integral part of daily life and revolutionized the way we communicate, retrieve information, and view entertainment. Between computers, televisions, mobile devices, electronic games, and even devices which measure metabolic rate. Electronic industry is the world’s largest and Innovative industry for its kind. Every year tons of electronic items are shipped over oceans, however, after their usage time they are become a complex waste matter which consists of many hazardous heavy metals, acids, toxic chemicals and non degradable plastics. Many are dumped, burnt or exported to recyclers. The Biogas produced by anaerobic digestion process has methane as its major constituent. 2.EXPERIMENTAL SETUP (Small Scale): Three different digesters were setup under different conditions with same initial composition were installed as below. The food waste used for the study in this project was collected from the mess at BIT Sindri. The food waste samples collected consisted of mixed wastes i.e., cooked wastes, uncooked wastes. The
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1757 indigestible wastes like onion peels, small twigs, egg shells, etc. were removed from the collected food wastes manually. Now electronic waste collected from BIT, Sindri campus. Sources of Electronic Waste in India The main sources of electronic waste in India are: A. Solder in printed circuit, glass panels & gaskets in Computer monitor B. Chip resistors & Semiconductors C. Refrigerators & Batteries D. Mobiles E. Microwave & Air Conditioners etc. Disposal Methods The toxic materials, which are used in manufacturing of Electronic good can damage to the environment. It contains Cathode ray tubes (crts), printed board assemblies, Capacitors, mercury switches and relays, batteries, liquid Crystal displays(lcds), cartridges from photocopying machines, selenium drums (photocopier) and electrolytes. The Disposal methods are as follows. Land filling- this method is suitable for quantitatively small e-waste i.e. domestic & small users. E -Waste is piled up & covered with other domestic waste & soil. Incineration- e-waste is burnt in controlled environment. The Toxic gases or smoke is released into atmosphere. Reuse-the spares &components are removed from the device & with some modification, they are used for other applications. Recycle-the important ingredients of e-waste is collected & sent to manufacturing companies producing similar components. The food wastes was then weighed 400gm for each setup. The food waste was crushed using a mixer grinder along with diluting it to 1 liter with water to form homogenized slurry(the food waste was diluted at a rate of 1:1.5 with water). The initial analysis of the food wastes before it was put into the reactor were performed, the same day it was collected from the hall. The analysis was done as follows.  The diluted food wastes collected on the 1st day were analyzed for Total Solids (TS), Volatile Solids (VS), Total Carbohydrates (TC) and pH.  The TS-VS content for each of the digester setup was measured every 5 days from the start of the setup.  The total Carbohydrate content for each of the digester setup was measured using
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1758 Phenol-Sulfuric acid method every 3 days from the start of the setup.  pH was measured every 2 days and was adjusted by adding sodium hydroxide to regulate the pH around 7.  Gas production of each setup was measured every day.  The substrate in the setup was kept well mixed by shaking the setup 4-5 times a day.  Hot water bath was used for heating and maintaining temperature during thermophilic stage. Materials Used for the setup:  3 separate 1.2 liter plastic bottles.  400 gm grinded kitchen waste diluted to 1 liter with water for each setup.  100ml diluted cow dung slurry was added and used as inoculums.  Rest space was left empty. Setup: 1. 400gm food waste diluted with water to make 1litre then 100ml diluted cow dung slurry was kept under mesophilic conditions at room temperature. pH of the setup was measured and adjusted to 6.6 initially. This setup was operated only for 20 days. Setup: 2. 400gm food waste diluted with water to make 1litre then 100ml diluted cow dung slurry. This setup was initially kept at thermophilic temperature (around 55° C) in a water bath for 2days and then under mesophilic conditions at room temperature and 50 ml more inoculums was added. pH of the setup was measured and adjusted to 6.7initially. This setup was operated only for 20 days. Setup: 3. 400gm food waste diluted with water to make 1litre then 100ml diluted cow dung slurry was kept under thermophilic temperature (around 55° C) in a water bath. pH of the setup was measured and adjusted to 6.5 initially. This setup was operated only for 10 days. 3.EXPERIMENTAL SETUP (Pilot Scale): The pilot scale biogas plant was made from the following components:- A. Inlet tank - From this tank the crushed food waste material was to be added. This part was made from a plastic bucket in which the slurry was prepared then added to the pre-digestion tank through the inlet of that pre-digester tank. Material used – Plastic Bucket (1 Nos.) B. Pre-digester tank - here the waste materials were heated around temperature of 50-60°C so
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1759 that thermophilic hydrolytic bacteria would grow. The substrate remained in this tank for 2 days. The heating helps in the faster digestion of the food waste. Material used – Steel Cylindrical Tank (10 Liters capacity, 1 Nos.) C. Main digestion tank – The waste materials after getting digested in the pre digester tanks for a 2 days was passed onto the main digester tank where the mesophilic methanogenic bacteria was allowed to grow with the addition of some new inoculums, which digest the food wastes further to produce methane gas. Material used – Steel Cylindrical Tank (20 Liters capacity, 1 Nos.) D. Gas collection unit – This unit was used to collect the gas that was generated from the digestion of the food wastes in the digester tanks. The gas was collected over water and was characterized to find the type of gas produced. Material used – Plastic bottles (2 Liters capacity, 2 Nos.) E. Slurry collection unit – This unit was be used to collect the digested slurry of the food wastes at regular intervals for the analysis. This slurry was be analyzed to study their characteristics. Material required – Plastic beakers (1 Nos.) Other Materials required – PVC pipes, silicon pipes and valves was be used to connect different units of the plant. Gas Production Table: Gas Production of the pilot scale setups with time Day Gas Production Day Gas Production 1 7200 14 7100 2 7050 15 7400 3 4850 16 7150 4 5000 17 7250 5 4800 18 7450 6 5540 19 7300 7 5750 20 7450 8 6200 21 7350 9 6250 22 7200 10 6350 23 7300 11 6150 24 7200 12 6850 25 7450 13 7150
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1760 4.Gas Analysis: Table: Gas analysis of the pilot scale setup with time Day H2(%) CO2(%) CH4(%) CO(%) O2(%) 5 3.11 66.2 0 0.01 6.22 10 0 70 1.2 0.01 8 18 0 56.12 10.2 0.01 8.21 25 0 45.3 18.56 0.01 6.41 5.CONCLUSION: The pilot scale plant was based on two stage thermophilic and mesophilic digestion process and operated as a batch reactor under controlled conditions of pH and temperature. A constant rate of gas production was achieved but accumulation of volatile fatty acids was also observed. In batch condition, it was observed that a maximum of 7.45 Liters biogas was produced from the digestion of 6 kg of food wastes in 25 days. Initially the total solids of the waste slurry was measured to be 10.27% on the day of starting the reactor and 5.51% on 25th day. The total carbohydrates degradation was measured to be 61.2 g/L on the day of starting the reactor and 22.3 g/L on 24th day. The volatile fatty acid concentration was measured as 2475.5 mg/L on the day of starting the reactor and 4954 mg/L on 24th day. The future prospect of the project can be the improvement of biogas production from kitchen wastes by incorporating additives and optimization of other process parameters in the two stage anaerobic digestion process. It is confirmed that the public awareness and co- operation of manufactures are essential for the advancement of e-waste management system. 0 10 20 30 40 50 60 70 80 5 10 18 25 Gas(%) Days Gas Analysis H2(%) CO2(%) CH4(%) CO(%) O2(%)
  • 7. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 02 | Feb -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 1761 Also e-wastes are the known major source of heavy metals, hazardous chemicals and carcinogens, certainly diseases related to skin, respiratory, intestinal, immune, and endocrine and nervous systems including cancers can be prevented by proper management and disposal of e-waste. 6.ACKNOWLEDGEMENT: I acknowledge Prof. Sunil Kumar, Mechanical Engineering department, BIT Sindri, Dhanbad for supporting me during completion of entire project. 7.REFERENCE: 1. Chanakya, H. and S. Malayil, Anaerobic digestion for bio-energy from agro-residues and other solid wastes—an overview of science, technology and sustainability. Journal of the Indian Institute of Science, 2012.92(1): p. 111-144. 2. Palaniswamy, D., et al. Experimental investigation of biogas production from food waste and analysis for the waste energy recovery and utilization from institutions of state of Tamil Nadu in India. in Intelligent Systems and Control (ISCO), 2013 7th International Conference on. 2013. IEEE. 3. Kale, S. and S. Mehetre, Kitchen waste based biogas plant. Nuclear Agriculture and Biotechnology Division, Bhabha Atomic Research Centre, India, 2006. 4. Fulekar, M., Environmental biotechnology. 2010: Science Publishers. 5. Salunkhe, D., R. Rai, and R. Borkar, BIOGAS TECHNOLOGY. International Journal of Engineering Science & Technology, 2012.4(12). 6.Vindis, P., et al., The impact of mesophilic and thermophilic anaerobic digestion on biogas production. Journal of achievements in materials and manufacturing Engineering, 2009.36(2): p. 192-198. 49 7.ATSDR (2007b) (cited in Kevin et al., 2008) (cited in Kevin et al., 2008) Toxicological Profile for lead. United States Public Health Service, Agency for Toxic Substances and Disease Registry, August 2007. 8. Basel Action uploaded on (2013) Exporting Harm: The High-Tech Trashing of Asia [video file] Retrieved fromhttp://www.youtube.com/watch?v=yDSWGV3j Gek 9. Lakshmi Raghupathy et.al, e-waste recycling in India –bridging the gap between the informal and formal sector. 10. Northeast Recycling Council (NERC). “Recycling Economic Information Study Update: Delaware, Maine, Massachusetts, New York, and Pennsylvania.” February 2009. Web. 6 June 2012.