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International Journal of Technical Research and Applications e-ISSN: 2320-8163,
www.ijtra.com Volume 2, Issue 5 (Sep-Oct 2014), PP. 67-70
67 | P a g e
ANAEROBIC DIGESTION OF MUNICIPAL
SOLID WASTE USING FUNGI CULTURE
(ASPERGILLUS FLAVUS ) WITH
METHANOGENS
Mahesh Kumar Shetty1
, Ravishankar R2
, Ramaraju H K3
,
1,2
Department Chemical Engineering, 3
Department of Civil Engineering,
1,2,3
Dayananda Sagar College of Engineering
Bangalore, Karnataka, India
1
maheshshetty20@gmail.com, 2
ravishankar70@gmail.com, 3
hkramaraju@gmail.com
Jagadish H Patil4
4
Assistant professor, Department of Chemical Engineering,
R.V. College of Engineering
Bangalore, Karnataka, India
4
patil_rvcechemical@rediffmail.com
Sunil H5
, Mamatha B.Salimath6
5
Department of Chemical Engineering, 6
Department of Microbiology,
Dayananda Sagar College of Engineering
Bangalore, Karnataka, India
5
coolsun33@gmail.com, 6
mamatha.mallik@gmail.com
Abstract— Municipal Solid Waste (MSW), mainly Kitchen Waste
(K) with Cow Dung (C) and Fungi Culture (F) can be used to
generate energy which could save on the fossil fuels conventionally
used as source of energy. In this study, the possibility was
explored to mix Cow Dung with Fungi Culture for anaerobic
digestion, so that energy can be generated as biogas and at the
same time digested sludge can be used as fertilizer for agricultural
applications. Pre-treatment of Kitchen Waste was done by alkali
method. Anaerobic digestion (AD) was carried out in mesophilic
temperature range of 30°C to 37°C with different fermentation
slurries of 8 % total solids. Digestion was carried for a retention
period of 60 days. The gas produced was collected by the
downward displacement of water and was subsequently measured
and analyzed. The overall results showed that blending of Kitchen
waste with cow dung and fungi culture (Aspergillus flavus) had
significant improvement on the biogas yield.
Keywords— Anaerobic Digestion, Cumulative Biogas Production,
Kitchen waste, Fungal Culture, Cow dung, Inoculums, Aspergillus
flavus.
I. INTRODUCTION
The country’s economy mainly depends on the energy
resources available and utilized. Energy has been exploited
since the prehistoric times. With the advent of industrial
revolution use of fossil fuels began growing and increasing till
date. The dependence on fossil fuel as primary energy source
has led to global climate change, environment degradation and
human health problems [1]. With increasing prices of oil and
gas the world looks towards alternative and green energy
resources. Anaerobic digestion (AD) offers a very attractive
route to utilize certain categories of biomass for meeting partial
energy needs. AD is a microbial decomposition of organic
matter into methane, carbon dioxide, inorganic nutrients and
compost in oxygen depleted environment and presence of the
hydrogen gas. This process is also known as bio-
methanogenesis. Anaerobic digestion has the advantage of
biogas production and can lead to efficient resource recovery
and contribution to the conservation of non-renewable energy
sources. AD can successfully treat the organic fraction of
biomass [2]. AD is the controlled degradation of biodegradable
waste in absence of oxygen and presence of different consortia
of bacteria that catalyze series of complex microbial reactions
[3]. The process is one of the most promising for biomass
wastes as it provides a source of energy while simultaneously
resolving ecological and agrochemical issues [4].
Fungi culture (Aspergillus flavus): A. flavus as well as some
other fungi, proved to have capacity of maturing in 3 days in an
anaerobic jar [5]. Fungi are found to be the major decomposers
of cellulose and lignin [6]. The production of cellulose enzyme
is a major factor in the hydrolysis of cellulosic materials [7].
Aspergillus flavus is capable of producing endoglucanase even
from sawdust and corncob. Aspergillus flavus also possess the
capacity to degrade the non- starch polysaccharide in the
substrate to soluble sugar [8]. Most of the cellulolytic
microorganisms belong to eubacteria and fungi can degrade
cellulose. Cellulolytic microorganisms can establish synergistic
relationships with non cellulolytic species in cellulosic wastes.
The interactions between both populations lead to complete
degradation of cellulose, releasing carbon dioxide and water
under aerobic conditions and carbon dioxide, methane and
water under anaerobic condition[9] The Strain Aspergillus
flavus can be recommended for bioremediation programmes to
clear cellulosic wastes [10].
II. MATERIALS AND METHODS
A. Sample Collection
Kitchen waste (K) was obtained from the canteen of
Dayananda Sagar College of Engineering, Bangalore. Fresh
cow dung was collected from a local cow yard in Yarab Nagar,
Bangalore. Fungal culture Aspergillus flavus was procured
from Department of Microbiology Culture Collection,
Bangalore University, Bangalore.
International Journal of Technical Research and Applications e-ISSN: 2320-8163,
www.ijtra.com Volume 2, Issue 5 (Sep-Oct 2014), PP. 67-70
68 | P a g e
B. Materials / Instruments
The materials/instruments used for the purpose of this
research are as follows: Weighing balance (Systronics), Gas
Chromatography (CHEMITO), pH meter (Systronics),
thermometer (range 0°C to 100°C), Borosilicate desiccators,
silica glass crucibles, oven, grinding mill, temperature
controlled water bath, water troughs, graduated transparent
glass gas collectors and biogas burner fabricated locally for
checking gas flammability. AR grade sodium hydroxide and
acetic acid manufactured by Ranbaxy laboratories were used as
procured without further purification.
C. Analytical Methods
The following parameters of Kitchen Waste and cow dung
were analyzed:
pH analysis: A glass electrode pH meter (Systronics) was
used to monitor the pH of the sample.
Total Solids (TS) and total volatile solids (VS) analysis: TS
were determined at 103°C to constant weight and VS were
measured by the loss on ignition of the dried sample at 550°C.
Biogas analysis: Gas Chromatograph (Chemito 1000)
equipped with a thermal conductivity detector was used to
analyze the biogas sample. Hydrogen was used as a carrier gas
(25 ml/min) with porapak Q column. Standard calibration gas
mixture was used for calibration. The oven temperature of
40°C, detection temperature of 80°C and the detector current of
180 mA were used.
D. Biomethanation Unit
A schematic diagram of biomethanation unit is shown in
Fig. 1 and water bath in Fig. 2. It consists of a temperature
controlled thermo bath which is maintained at 35°C [11] and
has a bio digester. Each bio digester is connected to a means of
connecting tube. A stand holds all the gas collectors. Biogas
evolved is collected by downward water displacement.
Fig. 1 Schematic picture of biomethanation unit
Fig. 2 Schematic picture of water bath
Fig. 3 Schematic diagram of water bath
E. Solid Analysis
Total solid (TS) and Volatile solid (VS) were analyzed for
Kitchen Waste and Cow Dung according to standard methods
[12]. Table.1 gives the solid analysis and pH data of Kitchen
Waste and Fungi Culture.
TABLE I
SOLID AND PH ANALYSIS
Digester pH % TS % VS
Kitchen Waste (K) 6.7 75.55 93.36
Cow Dung (C) 6.4 64.7 93.83
F. Fermentation Slurry Preparation
Fresh Kitchen Waste was initially collected and it was
grounded to paste in the mixer. Material balance was made and
different slurries with 8 % total solids were prepared by
varying the amount of paste (grounded kitchen waste) and
Water (W) [14]. The contents of each digester are shown in
Table 2. Each digester was checked for neutral pH (i.e., 7.0),
since the optimal pH for methanogenesis was found to be
around 7.0 [15] When measured, each digester was found to
have acidic pH (i.e., < 7.0), hence the contents were treated
with 1 % NaOH (by volume) solution to bring them to neutral
pH.
TABLE III
CONTENTS OF DIGESTERS
Digesters
Kitchen
waste (g)
Water (g)
Fungi
(g)
Cow
dung
(g)
DK 19.2 160.8 - -
DKF 19.2 160.8 5 -
DKC 19.2 160.8 - 2
DKCF 19.2 160.8 5 2
III. RESULTS AND DISCUSSION
A. The Influence of Inoculums to Cumulative Biogas
Productions
Anaerobic digestion of Kitchen Waste / Canteen Waste: The
quantity of cumulative biogas production with time for all the
digesters is given in Table 3. As shown in Fig. 3, Digesters DK,
DKF, DKC and DKCF commenced biogas production from 5th
day and evolved flammable biogas from 9th
day. While digester
Kitchen Waste Blank which serves as blank for Kitchen waste
International Journal of Technical Research and Applications e-ISSN: 2320-8163,
www.ijtra.com Volume 2, Issue 5 (Sep-Oct 2014), PP. 67-70
69 | P a g e
commenced biogas production after 10 days and evolved
flammable biogas on 20th
day. The highest biogas yield was for
digester DKCF (0.28 l/gVS). This performance could be
because of optimum balance between the anaerobic bacteria
consortium and amount of VS (23.76 g). This indicates
digestion of Kitchen Waste and cow dung with fungi culture
improves biogas yield significantly.
TABLE IIIII
CUMULATIVE BIOGAS PRODUCTION
Days DK
(l/g VS)
DKF
(l/g VS)
DKC
(l/g VS)
DKCF
(l/g VS)
0 0 0 0 0
5 0 0.006 0.005 0.01
10 0.001 0.011 0.01 0.02
15 0.005 0.045 0.04 0.06
20 0.008 0.075 0.07 0.08
25 0.012 0.115 0.1 0.12
30 0.021 0.15 0.14 0.17
35 0.045 0.18 0.17 0.21
40 0.075 0.2 0.19 0.24
45 0.115 0.22 0.21 0.26
50 0.15 0.23 0.22 0.28
55 0.16 0.235 0.23 0.28
60 0.17 0.24 0.23 0.28
Fig. 3 Daily biogas production
B. Analysis of Biogas
With Biogas analysis was done for chief components CH4
and CO2 for biogas evolved from the digester DKCF. Biogas
was sampled in a rubber bladder carefully. Gas chromatograph
(Chemito 1000) equipped with a thermal conductivity detector
was used to analyze the biogas sample. Hydrogen was used as
carrier gas (25 ml/min) with Porapak Q column. Standard gas
mixture was used for calibration. A fixed 500 μl volume was
taken each time using a gastight syringe. The sample was then
injected to gas chromatograph to analyze for methane and
carbon dioxide. Following are the characteristics of the GC gas
composition method:
Column : Porapak Q
Gas : Hydrogen with flow rate of 25 ml/min
Oven : 40°C
Detector : TCD at 80°C and 180 mA
The concentrations of methane and carbon dioxide were
calculated using
The gas chromatogram obtained is shown in Fig. 4. The
amounts of CH4, CO2 and CO in the biogas were found to be
59.3 %, 40.6 % and 0.1 % respectively. The biogas
compositions from the other digesters were also found to be in
the same range.
Fig. 4 Gas chromatogram for the digester DKCF
IV.CONCLUSIONS
Kitchen Waste is a very good biogas producer, needs
minimal pre-treatment (soaking in NaOH solution and
grinding) to enhance the biogas yield. The use of Cow dung
with Fungi culture (Aspergillus flavus) for biogas generation
therefore, will be a good energy source. The result of the study
has shown that anaerobic digestion of ground Kitchen waste
with cow dung and Aspergillus flavus improved biogas yield.
This performance confirms the earlier reports by other
researchers that combining cow dung with fungi culture
catalyzes the biogas production with consequent increased
yield [16].
ACKNOWLEDGEMENT
We thankfully acknowledge the help from Prof. Karthik K.V,
Prof. D.C Sikdar, Prof. G.K Mahadevaraju, Prof. B.S.
Thirumalesh, Prof. Pradeep H.N, Prof. S.C Maidargi, Prof.
S.M. Desai, Department of Chemical Engineering, DSCE,
Bangalore and the entire staff of the Department of Chemical
Engineering, DSCE, Bangalore and authorities of Dayananda
Sagar College of Engineering, Bangalore.
REFERENCES
[1] Budiyano, Widiasa I N, Johari and Sunarso S Increasing biogas
production rate from cattle manure using rumen fluid as
inoculums, International Journal of Chemical and Basic &
Applied Sciences, 10(1), 68-75, 2010
[2] Hill DT Simplified Monod kinetics of methane fermentation of
animal wastes, Agricultural Wastes, 5, 1–16, 1983
[3] McInerney M J. Bryant M P and Stafford D A Metabolic stages
and energetics of microbial anaerobic digestion. In: Stafford DA,
Wheatley BI, Hudges DE (eds) Anaerobic digestion, Applied
Science, London, 91-98, 1980.
International Journal of Technical Research and Applications e-ISSN: 2320-8163,
www.ijtra.com Volume 2, Issue 5 (Sep-Oct 2014), PP. 67-70
70 | P a g e
[4] Budiyano, Widiasa I N, Johari and Sunarso S The kinetic of
biogas production rate from cattle manure in batch mode,
International Journal of Chemical and Biomolecular
Engineering, 3(1), 39-44, 2010
[5] Gunnel Clevstrom, Hans Ljunggren,Seven Tegelstrom, and
Kerstin Tideman Production of aflattoxin by an A. Flavus Isolate
culture under limited oxygen supply. Applied and Environmental
Microbiology Aug Vol 46 No.2, 400-40. 1983
[6] Bennett JW., A Childress and K Wunch Fungi in bioremediation.
Int. Biodet Biodeger 37: 244-255,1996.
[7] Ghose, TK Measurement of cellulose activities. Pure Applied
Chem 59: 257-268,1987.
[8] Hamyln, P.F Fungal biotechnology. Br.Mycol.Soc Newslett 30:
930-934,1998
[9] Leschine, S.B Cellulose degradation in anaerobic environments
Annu. Rev Microbiol 49: 399-426
[10] Betty Anitha B, Thatheyus A.J and Ramya D [2013]
Biodegradation of Caroboxymethyl Cellulose using Aspergillus
flavus. Science international DOI 10.5567/sciintl.85.91, 85-
91,1995.
[11] Chae, K.J., Jang, A., Yim, S.K., Kim, I.S., The effects of
digestion temperature and temperature shock on the biogas yields
from the mesophilic anaerobic digestion of swine manure.
Bioresour. Technol. 99, 1–6. 2008
[12] APHA, AWWA and WPCF Standard methods for the
examination of water and waste water, Washington D.C, 19,1995
[13] Jagadish. Patil. H, Antony Raj MAL and Gavimath CStudy on
effect of pretreatment methods on biomethanation of water
hyacinth. International Journal of Advanced Biotechnology and
Research, 2(1), 143-147,2011.
[14] Jagadish Patil H, Antony Raj MAL, Shankar BB, Mahesh Kumar
Shetty, and Pradeep Kumar B P. Anaerobic Co-Digestion of
Water Hyacinth and Sheep Waste. International Conference on
Alternative Energy in Developing Countries and Emerging
Economies. 216-220,2013
[15] Yang, S.T, Okos, M.R Kinetic study and mathematical modeling
of methanogenesis of acetate using pure cultures of methanogens.
Biotechnol Bioeng. 30, 661–667,1987
[16] Huber, H., Thomm, M., Konig, H., Thies, G., Stetter, K.O
Methanococeus thermolithotrophicus, a novel thermophilic
lithotrophic methanogen. Arch. Microbiol. 132, 47–50, 1982
AUTHORS
First Author – Mahesh Kumar Shetty, B.E, M.Sc, (M.Sc
(Engg)), DSCE, Bangalore and maheshshetty20@gmail.com.
Second Author – Ravishankar R, Ph.D., DSCE, Bangalore and
ravishankar70@gmail.com.
Third Author – Ramaraju H K, Ph.D., DSCE, Bangalore and
hkramaraju@gmail.com.
Fourth Author – Jagadish H Patil, Ph.D., RVCE, Bangalore
and patil_rvcechemical@rediffmail.com
Fifth Author – Sunil H, M.Tech, DSCE, Bangalore and
coolsun33@gmail.com
Sixth Author – Mamatha B.Salimath, M.Sc, M.Ed, M.Phil,
(Ph.D) DSCE, Bangalore and mamatha.mallik@gmail.com

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ANAEROBIC DIGESTION OF MUNICIPAL SOLID WASTE USING FUNGI CULTURE (ASPERGILLUS FLAVUS ) WITH METHANOGENS

  • 1. International Journal of Technical Research and Applications e-ISSN: 2320-8163, www.ijtra.com Volume 2, Issue 5 (Sep-Oct 2014), PP. 67-70 67 | P a g e ANAEROBIC DIGESTION OF MUNICIPAL SOLID WASTE USING FUNGI CULTURE (ASPERGILLUS FLAVUS ) WITH METHANOGENS Mahesh Kumar Shetty1 , Ravishankar R2 , Ramaraju H K3 , 1,2 Department Chemical Engineering, 3 Department of Civil Engineering, 1,2,3 Dayananda Sagar College of Engineering Bangalore, Karnataka, India 1 maheshshetty20@gmail.com, 2 ravishankar70@gmail.com, 3 hkramaraju@gmail.com Jagadish H Patil4 4 Assistant professor, Department of Chemical Engineering, R.V. College of Engineering Bangalore, Karnataka, India 4 patil_rvcechemical@rediffmail.com Sunil H5 , Mamatha B.Salimath6 5 Department of Chemical Engineering, 6 Department of Microbiology, Dayananda Sagar College of Engineering Bangalore, Karnataka, India 5 coolsun33@gmail.com, 6 mamatha.mallik@gmail.com Abstract— Municipal Solid Waste (MSW), mainly Kitchen Waste (K) with Cow Dung (C) and Fungi Culture (F) can be used to generate energy which could save on the fossil fuels conventionally used as source of energy. In this study, the possibility was explored to mix Cow Dung with Fungi Culture for anaerobic digestion, so that energy can be generated as biogas and at the same time digested sludge can be used as fertilizer for agricultural applications. Pre-treatment of Kitchen Waste was done by alkali method. Anaerobic digestion (AD) was carried out in mesophilic temperature range of 30°C to 37°C with different fermentation slurries of 8 % total solids. Digestion was carried for a retention period of 60 days. The gas produced was collected by the downward displacement of water and was subsequently measured and analyzed. The overall results showed that blending of Kitchen waste with cow dung and fungi culture (Aspergillus flavus) had significant improvement on the biogas yield. Keywords— Anaerobic Digestion, Cumulative Biogas Production, Kitchen waste, Fungal Culture, Cow dung, Inoculums, Aspergillus flavus. I. INTRODUCTION The country’s economy mainly depends on the energy resources available and utilized. Energy has been exploited since the prehistoric times. With the advent of industrial revolution use of fossil fuels began growing and increasing till date. The dependence on fossil fuel as primary energy source has led to global climate change, environment degradation and human health problems [1]. With increasing prices of oil and gas the world looks towards alternative and green energy resources. Anaerobic digestion (AD) offers a very attractive route to utilize certain categories of biomass for meeting partial energy needs. AD is a microbial decomposition of organic matter into methane, carbon dioxide, inorganic nutrients and compost in oxygen depleted environment and presence of the hydrogen gas. This process is also known as bio- methanogenesis. Anaerobic digestion has the advantage of biogas production and can lead to efficient resource recovery and contribution to the conservation of non-renewable energy sources. AD can successfully treat the organic fraction of biomass [2]. AD is the controlled degradation of biodegradable waste in absence of oxygen and presence of different consortia of bacteria that catalyze series of complex microbial reactions [3]. The process is one of the most promising for biomass wastes as it provides a source of energy while simultaneously resolving ecological and agrochemical issues [4]. Fungi culture (Aspergillus flavus): A. flavus as well as some other fungi, proved to have capacity of maturing in 3 days in an anaerobic jar [5]. Fungi are found to be the major decomposers of cellulose and lignin [6]. The production of cellulose enzyme is a major factor in the hydrolysis of cellulosic materials [7]. Aspergillus flavus is capable of producing endoglucanase even from sawdust and corncob. Aspergillus flavus also possess the capacity to degrade the non- starch polysaccharide in the substrate to soluble sugar [8]. Most of the cellulolytic microorganisms belong to eubacteria and fungi can degrade cellulose. Cellulolytic microorganisms can establish synergistic relationships with non cellulolytic species in cellulosic wastes. The interactions between both populations lead to complete degradation of cellulose, releasing carbon dioxide and water under aerobic conditions and carbon dioxide, methane and water under anaerobic condition[9] The Strain Aspergillus flavus can be recommended for bioremediation programmes to clear cellulosic wastes [10]. II. MATERIALS AND METHODS A. Sample Collection Kitchen waste (K) was obtained from the canteen of Dayananda Sagar College of Engineering, Bangalore. Fresh cow dung was collected from a local cow yard in Yarab Nagar, Bangalore. Fungal culture Aspergillus flavus was procured from Department of Microbiology Culture Collection, Bangalore University, Bangalore.
  • 2. International Journal of Technical Research and Applications e-ISSN: 2320-8163, www.ijtra.com Volume 2, Issue 5 (Sep-Oct 2014), PP. 67-70 68 | P a g e B. Materials / Instruments The materials/instruments used for the purpose of this research are as follows: Weighing balance (Systronics), Gas Chromatography (CHEMITO), pH meter (Systronics), thermometer (range 0°C to 100°C), Borosilicate desiccators, silica glass crucibles, oven, grinding mill, temperature controlled water bath, water troughs, graduated transparent glass gas collectors and biogas burner fabricated locally for checking gas flammability. AR grade sodium hydroxide and acetic acid manufactured by Ranbaxy laboratories were used as procured without further purification. C. Analytical Methods The following parameters of Kitchen Waste and cow dung were analyzed: pH analysis: A glass electrode pH meter (Systronics) was used to monitor the pH of the sample. Total Solids (TS) and total volatile solids (VS) analysis: TS were determined at 103°C to constant weight and VS were measured by the loss on ignition of the dried sample at 550°C. Biogas analysis: Gas Chromatograph (Chemito 1000) equipped with a thermal conductivity detector was used to analyze the biogas sample. Hydrogen was used as a carrier gas (25 ml/min) with porapak Q column. Standard calibration gas mixture was used for calibration. The oven temperature of 40°C, detection temperature of 80°C and the detector current of 180 mA were used. D. Biomethanation Unit A schematic diagram of biomethanation unit is shown in Fig. 1 and water bath in Fig. 2. It consists of a temperature controlled thermo bath which is maintained at 35°C [11] and has a bio digester. Each bio digester is connected to a means of connecting tube. A stand holds all the gas collectors. Biogas evolved is collected by downward water displacement. Fig. 1 Schematic picture of biomethanation unit Fig. 2 Schematic picture of water bath Fig. 3 Schematic diagram of water bath E. Solid Analysis Total solid (TS) and Volatile solid (VS) were analyzed for Kitchen Waste and Cow Dung according to standard methods [12]. Table.1 gives the solid analysis and pH data of Kitchen Waste and Fungi Culture. TABLE I SOLID AND PH ANALYSIS Digester pH % TS % VS Kitchen Waste (K) 6.7 75.55 93.36 Cow Dung (C) 6.4 64.7 93.83 F. Fermentation Slurry Preparation Fresh Kitchen Waste was initially collected and it was grounded to paste in the mixer. Material balance was made and different slurries with 8 % total solids were prepared by varying the amount of paste (grounded kitchen waste) and Water (W) [14]. The contents of each digester are shown in Table 2. Each digester was checked for neutral pH (i.e., 7.0), since the optimal pH for methanogenesis was found to be around 7.0 [15] When measured, each digester was found to have acidic pH (i.e., < 7.0), hence the contents were treated with 1 % NaOH (by volume) solution to bring them to neutral pH. TABLE III CONTENTS OF DIGESTERS Digesters Kitchen waste (g) Water (g) Fungi (g) Cow dung (g) DK 19.2 160.8 - - DKF 19.2 160.8 5 - DKC 19.2 160.8 - 2 DKCF 19.2 160.8 5 2 III. RESULTS AND DISCUSSION A. The Influence of Inoculums to Cumulative Biogas Productions Anaerobic digestion of Kitchen Waste / Canteen Waste: The quantity of cumulative biogas production with time for all the digesters is given in Table 3. As shown in Fig. 3, Digesters DK, DKF, DKC and DKCF commenced biogas production from 5th day and evolved flammable biogas from 9th day. While digester Kitchen Waste Blank which serves as blank for Kitchen waste
  • 3. International Journal of Technical Research and Applications e-ISSN: 2320-8163, www.ijtra.com Volume 2, Issue 5 (Sep-Oct 2014), PP. 67-70 69 | P a g e commenced biogas production after 10 days and evolved flammable biogas on 20th day. The highest biogas yield was for digester DKCF (0.28 l/gVS). This performance could be because of optimum balance between the anaerobic bacteria consortium and amount of VS (23.76 g). This indicates digestion of Kitchen Waste and cow dung with fungi culture improves biogas yield significantly. TABLE IIIII CUMULATIVE BIOGAS PRODUCTION Days DK (l/g VS) DKF (l/g VS) DKC (l/g VS) DKCF (l/g VS) 0 0 0 0 0 5 0 0.006 0.005 0.01 10 0.001 0.011 0.01 0.02 15 0.005 0.045 0.04 0.06 20 0.008 0.075 0.07 0.08 25 0.012 0.115 0.1 0.12 30 0.021 0.15 0.14 0.17 35 0.045 0.18 0.17 0.21 40 0.075 0.2 0.19 0.24 45 0.115 0.22 0.21 0.26 50 0.15 0.23 0.22 0.28 55 0.16 0.235 0.23 0.28 60 0.17 0.24 0.23 0.28 Fig. 3 Daily biogas production B. Analysis of Biogas With Biogas analysis was done for chief components CH4 and CO2 for biogas evolved from the digester DKCF. Biogas was sampled in a rubber bladder carefully. Gas chromatograph (Chemito 1000) equipped with a thermal conductivity detector was used to analyze the biogas sample. Hydrogen was used as carrier gas (25 ml/min) with Porapak Q column. Standard gas mixture was used for calibration. A fixed 500 μl volume was taken each time using a gastight syringe. The sample was then injected to gas chromatograph to analyze for methane and carbon dioxide. Following are the characteristics of the GC gas composition method: Column : Porapak Q Gas : Hydrogen with flow rate of 25 ml/min Oven : 40°C Detector : TCD at 80°C and 180 mA The concentrations of methane and carbon dioxide were calculated using The gas chromatogram obtained is shown in Fig. 4. The amounts of CH4, CO2 and CO in the biogas were found to be 59.3 %, 40.6 % and 0.1 % respectively. The biogas compositions from the other digesters were also found to be in the same range. Fig. 4 Gas chromatogram for the digester DKCF IV.CONCLUSIONS Kitchen Waste is a very good biogas producer, needs minimal pre-treatment (soaking in NaOH solution and grinding) to enhance the biogas yield. The use of Cow dung with Fungi culture (Aspergillus flavus) for biogas generation therefore, will be a good energy source. The result of the study has shown that anaerobic digestion of ground Kitchen waste with cow dung and Aspergillus flavus improved biogas yield. This performance confirms the earlier reports by other researchers that combining cow dung with fungi culture catalyzes the biogas production with consequent increased yield [16]. ACKNOWLEDGEMENT We thankfully acknowledge the help from Prof. Karthik K.V, Prof. D.C Sikdar, Prof. G.K Mahadevaraju, Prof. B.S. Thirumalesh, Prof. Pradeep H.N, Prof. S.C Maidargi, Prof. S.M. Desai, Department of Chemical Engineering, DSCE, Bangalore and the entire staff of the Department of Chemical Engineering, DSCE, Bangalore and authorities of Dayananda Sagar College of Engineering, Bangalore. REFERENCES [1] Budiyano, Widiasa I N, Johari and Sunarso S Increasing biogas production rate from cattle manure using rumen fluid as inoculums, International Journal of Chemical and Basic & Applied Sciences, 10(1), 68-75, 2010 [2] Hill DT Simplified Monod kinetics of methane fermentation of animal wastes, Agricultural Wastes, 5, 1–16, 1983 [3] McInerney M J. Bryant M P and Stafford D A Metabolic stages and energetics of microbial anaerobic digestion. In: Stafford DA, Wheatley BI, Hudges DE (eds) Anaerobic digestion, Applied Science, London, 91-98, 1980.
  • 4. International Journal of Technical Research and Applications e-ISSN: 2320-8163, www.ijtra.com Volume 2, Issue 5 (Sep-Oct 2014), PP. 67-70 70 | P a g e [4] Budiyano, Widiasa I N, Johari and Sunarso S The kinetic of biogas production rate from cattle manure in batch mode, International Journal of Chemical and Biomolecular Engineering, 3(1), 39-44, 2010 [5] Gunnel Clevstrom, Hans Ljunggren,Seven Tegelstrom, and Kerstin Tideman Production of aflattoxin by an A. Flavus Isolate culture under limited oxygen supply. Applied and Environmental Microbiology Aug Vol 46 No.2, 400-40. 1983 [6] Bennett JW., A Childress and K Wunch Fungi in bioremediation. Int. Biodet Biodeger 37: 244-255,1996. [7] Ghose, TK Measurement of cellulose activities. Pure Applied Chem 59: 257-268,1987. [8] Hamyln, P.F Fungal biotechnology. Br.Mycol.Soc Newslett 30: 930-934,1998 [9] Leschine, S.B Cellulose degradation in anaerobic environments Annu. Rev Microbiol 49: 399-426 [10] Betty Anitha B, Thatheyus A.J and Ramya D [2013] Biodegradation of Caroboxymethyl Cellulose using Aspergillus flavus. Science international DOI 10.5567/sciintl.85.91, 85- 91,1995. [11] Chae, K.J., Jang, A., Yim, S.K., Kim, I.S., The effects of digestion temperature and temperature shock on the biogas yields from the mesophilic anaerobic digestion of swine manure. Bioresour. Technol. 99, 1–6. 2008 [12] APHA, AWWA and WPCF Standard methods for the examination of water and waste water, Washington D.C, 19,1995 [13] Jagadish. Patil. H, Antony Raj MAL and Gavimath CStudy on effect of pretreatment methods on biomethanation of water hyacinth. International Journal of Advanced Biotechnology and Research, 2(1), 143-147,2011. [14] Jagadish Patil H, Antony Raj MAL, Shankar BB, Mahesh Kumar Shetty, and Pradeep Kumar B P. Anaerobic Co-Digestion of Water Hyacinth and Sheep Waste. International Conference on Alternative Energy in Developing Countries and Emerging Economies. 216-220,2013 [15] Yang, S.T, Okos, M.R Kinetic study and mathematical modeling of methanogenesis of acetate using pure cultures of methanogens. Biotechnol Bioeng. 30, 661–667,1987 [16] Huber, H., Thomm, M., Konig, H., Thies, G., Stetter, K.O Methanococeus thermolithotrophicus, a novel thermophilic lithotrophic methanogen. Arch. Microbiol. 132, 47–50, 1982 AUTHORS First Author – Mahesh Kumar Shetty, B.E, M.Sc, (M.Sc (Engg)), DSCE, Bangalore and maheshshetty20@gmail.com. Second Author – Ravishankar R, Ph.D., DSCE, Bangalore and ravishankar70@gmail.com. Third Author – Ramaraju H K, Ph.D., DSCE, Bangalore and hkramaraju@gmail.com. Fourth Author – Jagadish H Patil, Ph.D., RVCE, Bangalore and patil_rvcechemical@rediffmail.com Fifth Author – Sunil H, M.Tech, DSCE, Bangalore and coolsun33@gmail.com Sixth Author – Mamatha B.Salimath, M.Sc, M.Ed, M.Phil, (Ph.D) DSCE, Bangalore and mamatha.mallik@gmail.com