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International Journal of Trend in Scientific Research and Development (IJTSRD)
Volume: 3 | Issue: 2 | Jan-Feb 2019 Available Online: www.ijtsrd.com e-ISSN: 2456 - 6470
@ IJTSRD | Unique Reference Paper ID – IJTSRD21410 | Volume – 3 | Issue – 2 | Jan-Feb 2019 Page: 455
Performance Evaluation of the Effect of pH and
Temperature on the Biogas Yield of Co-Digestion
of Pig Manure and Water Hyacinth
Nse Peter Essang
Department of Petroleum and Natural Gas Processing Engineering,
Petroleum Training Institute, Effurun, Nigeria
ABSTRACT
In this research work, the effect of pH and temperature on the biogas yield of co-digestion of Pig manure and water hyacinth
were investigated experimentally in laboratoryscale anaerobicbioreactors.Theco-digestionwasrun foraHydraulicRetention
Time thirty six days. The volumetric yield of biogas was noted once there is biogas build up at regular intervals using water
displacement method. A total of ten evacuations were made and the data obtained was used to evaluate the effect of the
aforementioned anaerobic digestion parameters. The experimental results revealed that a neutral pH value of 7 yielded
optimum biogas yields compared to a pH value above and below 7. Moreover, from all the experimental mesophilic
temperature used in this research work, an optimum mesophilic temperature of 37 oC favoured the optimum biogas yield.
KEYWORDS: pH, Biogas yield, Hydraulic retention time, Pig manure, Water Hyacinth, Optimum biogas yield
1. INTRODUCTION
The increasing demand for energy,inadequateavailabilityof
conventional energy supplied such as fossil and wood fuel
resources, increase in crude oil prices, and the increasing
concern for environmental issues have challenged
researchers across the world to develop an alternative
energy means that is clean and sustainable energy through
the utilization of non-conventional renewable energy
sources [1-4]. In this respect, biogas production from
anaerobic digestion or co-digestionprocessof biodegradable
organic waste will be a welcome development. The
anaerobic digestion (AD) process has become an
increasingly vital industrial process. The production of
biogas from AD process is of growing interest across the
world [5-7] and this is due to decline in wood and fossil fuel
resources and their resulting effect on the ozone layer [8].
Worldwide greenhouse gas (GHG) emissions from biomass
have doubled since the 1960s and could further increase by
30% if nothing is done about it. Anaerobic digestion is
widely as a treatment option for the disposal of municipal
solid waste on a par with the composting technologies. It
mainly combines with the energy recovery benefits,
greenhouse gas mitigation and produces stable end
products, which can be furtherupgradedascompostforland
use applications [9].
To optimize the rate of biogas yield, itis essentialtooptimize
the process parameters involved in the digestion process.
Many researchers investigated the effects of process
parameters involved in the biogas production and reported
their findings. Orhorhoro et al. [10] investigated the effect
organic loading rate (OLR) on biogas yield from food waste,
water hyacinth, and cow dung, waste water from abattoir,
poultry dropping and pig dung. Their experiment was
conducted within a mesophilic temperature range of 360C-
370C, percentage total solid (%TS) of 9.98% and percentage
volatile solid (%VS) of 78%. pH meter was used to
monitored the daily pH reading of the slurry. They reported
that the quantity of biogas yieldfromthefeedstock increases
with increasing organic load rate totheoptimum valueof 1.5
kg/m3 and started decreasing above theoptimum valuefora
single stage AD reactor for a three-stages continuous AD
reactors there was a continuousincreaseinbiogasyield with
a successive increase in OLR from 1-5 kg/m3-3.0 kg/m3.
Sivakumar et al. [11] investigated the effect of pH using
spoiled milk as substrate and reported that the substrate
with 7 pH resulted better biogas yield. Kafle et al [12]
investigated the effect of co-digestion of Kimchi factory
waste silage and swine manure under mesophilic
temperature condition. The results suggested that Kimchi
factory waste could be effectively treated by making silage,
and the silage could be used as a potential co-substrate to
enhance biogas production from swine manure digester.
Deepanraj et al. [13] studied the effect of temperature on
biogas production using food waste in a lab scale batch
reactor and found that the operating temperature of 50°C
achieved maximum biogas yield. Orhorhoro et al. [14]
analyzed of the effect of Carbon/Nitrogen (C/N) ratio on the
performance of biogas yields for non-uniform multiple feed
stock availability and composition in Nigeria. The results
obtained from their research work show that C/N ratio of
substrates affects hydraulic retention time, biogas yield and
the rate of frequency of evacuation. Therefore, for a better
biogas yield, combination of low and high C/N ratio
substrates is recommended. Sumardiono et al. [15]
investigated the effect of COD/N ratios of substrate and pH
control to biogas production from vinasse. Their study used
anaerobic digestion-laboratoryscaleatroomtemperaturein
batch system. Urea was added as nitrogen source to adjust
COD/N ratios of 400/7, 500/7, 600/7, and 700/7. Initial pH
for all variables was adjusted 7.0 by using NaOH solution.
The results obtained reveal that biogas formed at COD/N
ratio of control variable (1436/7); 400/7; 500/7; 600/7;
700/7 were 3.673; 4.909; 6.079; 6.096; 5.631 mL/g COD
respectively. pH profiles for all variables were decreasing
from beginning until endingof fermentation. With controlled
pH, pH of substrates was maintained at neutral condition,so
methanogenic bacteria could grow well in the digesters.
Consequently biogas formed at controlled pH was larger
International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Reference Paper ID – IJTSRD21410 | Volume – 3 | Issue – 2 | Jan-Feb 2019 Page: 456
than that at uncontrolled pH. The values of COD removal for
COD/N ratio of control variable; 400/7; 500/7; 600/7;
700/7 were 1.27±0.43; 1.59±0.43; 2.85±0.39; 3.21±0.49;
2.22±0.39 % respectively at uncontrolled pH, whereas at
controlled pH the values of these were 11.98±0.56;
12.82±0.56; 12.03±0.94; 13.05±0.35; 12.61±0.56 %
respectively. However, enough research works were not
reported on biogas yield performance of co-digestion of
animal manure and seed weeds, thus this research work.
2. Materials and Methods
Water hyacinth used in this research work was harvested
from River Ethiope, Boboroku- Jesse, Nigeria (Figure 1), and
the Pig manure collected from Pig farm, Jesse, Nigeria
(Figure 2). The experiment was carried out in laboratory-
scale reactors as depicted in the schematic diagram (Figure
3). The volume of each reactor was 2,000 ml with a working
volume of 1250 ml. All the reactors were purged with
nitrogen before start-up in order to create anaerobic
condition. The mixing was continuous and thiswasachieved
using magnetic stirrer. The experiment was subjected to
mesophilic temperature range of 36 0C as recommended by
Ebunilo et al. [2]. A pH meter wasmonitoredusingelectronic
pH metering (Figure 4).
Figure 1: Water Hyacinth
Figure 2: Pig Manure
Figure 3: Experimental Setup
Figure 4: pH Meter
3. Results and Discussion
The roots of the water hyacinth were gently detached and
the remaining parts properly washed and grinded using a
grinding machine. The grinded water hyacinth was co-
digested with the Pig manure to form slurry. According to
Orhorhoro et al., [16], grinding increased the surface area of
contact for the microbial activity, so that biogas yield would
start within the shortest possible time. Preparation of
fermentation of slurry was by addition and vigorous mixing
of total substrate with an equivalent amount of water
needed for maximum yield. The ratio of total substrate to
water was 1:2 as recommended by Ebunilo et al., [17]. The
amount of biogas yield was measured once there is an
indication of biogas build up in the measuring cylinder. The
measuring cylinder was then inverted with the gas pressure
displacing equal amount of water and the readings were
recorded. This procedure was repeated ten (10) times to
ascertain the total volume of biogas produced. A pH meter
was used to monitor the pH of the system. To measure the
pH of the slurry, the probe (glass electrode) was inserted
into the sample of the slurry after each evacuation. The
results obtained show that optimum biogas yield was
obtained at pH neutral reading of 7. Furthermore, a pH
values below and above the optimum biogas yielding pH
value of 7 brings about drops in biogas yield.
Figure 5: Results of Performance Evaluation
International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470
@ IJTSRD | Unique Reference Paper ID – IJTSRD21410 | Volume – 3 | Issue – 2 | Jan-Feb 2019 Page: 457
It was also observed that temperature affect the biogas yield
throughout the hydraulic retention time. Anoptimumbiogas
yields was obtained at optimum mesophilic temperature of
37 oC, and this agree with the research work of Ebunilo et al.
[2].
4. Conclusion
In this research work, the effect of pH and temperature on
biogas yield from co-digestion of Pig manure and water
hyacinth were successfully evaluated The results obtained
from the research work show that an optimum biogas yield
is favored with a slurry pH of neutralityvalueof7.Moreover,
for an optimum biogas yield, an optimum mesophilic
temperature is required. Besides, the abundant water
hyacinth in River Ethiope and Pig manure in Jesse can be
used for production of biogas which can be used in place of
conventional energy such as wood and fossil fuel.
References
[1] E. K. Orhorhoro, P. O. Ebunilo, E. G. Sadjere.
Development of a Predictive Model for Biogas Yield
Using Artificial Neural Networks (ANNs) Approach.
American Journal of Energy and Power Engineering,
2017; 4(6): 71-77
[2] P. O. Ebunilo, E. K. Orhorhoro, V. Oboh, P. U. Onochie.
Effect of Temperature on Biogas Yields Using South-
South Nigeria as a Case Study. International Journal of
Technology Enhancements and Emerging Engineering
Research, 2016, 4(3), pp. 50-54
[3] E. K. Orhorhoro, O. W. Orhorhoro, A. E. Ikpe. A Study of
Solar Energy Potential in Sapele, Nigeria. Int. J. of
Thermal & Environmental Engineering, 13(2), 2016,
129-133
[4] G. K. Kafle, S. Bhattarai, S.H. Kim, L. Chen, Anaerobic
digestion of Chinese cabbage waste silage with swine
manure for biogas production: batch and continuous
study, Environmental Technology, 35, 2014, 2708–
2717.
[5] E. K. Orhorhoro, P. O. Ebunilo, E. G. Sadjere.
Experimental Determination of Effect of Total Solid
(TS) and Volatile Solid (VS) on Biogas Yield. American
Journal of Modern Energy, 2017, 3(6): 131-135
[6] W. Qiao, X. Yan, J. Ye, Y. Sun, W. Wang, Z. Zhang.
Evaluation of biogas productio from different biomass
wastes with/without hydrothermal pretreatment.
Renewable Energy, 36, 2011, 3313-3318
[7] T. Subramani, M. Nallathambi. Mathematical Model for
Commercial Production of Bio-Gas fromSewageWater
and Kitchen Waste. International Journal of Modern
Engineering Research (IJMER), 2 (4),2012,1588-1595
[8] P. O. Osunde, P. O. B Ebunilo, E. K. Orhorhoro.
Preliminary Evaluation of a Biogas Purification Filter
Suitable for use in Nigeria Journal of Scientific and
Engineering Research, 2017, 4(10), 125-134
[9] E. Dogan, G.N. Demirer, Biogas generation by two-
phase anaerobic digestion of organic fraction of
municipal solid waste, Journal of Renewable &
Sustainable Energy, 4, 2012, 063131
[10] E. K. Orhorhoro, P.O. Ebunilo, E. G. Sadjere. Effect of
Organic Loading Rate (OLR) on Biogas Yield Using a
Single and Three-Stages Continuous Anaerobic
Digestion Reactors. International Journal of
Engineering Research in Africa, Vol. 39, pp. 147-155
[11] H. Raheman, S. Mondal, Biogas production potential of
jatropha seed cake, Biomass and Bioenergy, 37, 2012,
pp.25-30.
[12] P. Sivakumar, M. Bhagiyalakshmi, and K. Anbarasu,
Anaerobic treatment of spoiled milk from milk
processing industryforenergyrecovery—A laboratory
to pilot scale study, Fuel, 96, 2012, 482–486.
[13] G. K. Kafle, S.H. Kim, Sung, Batch anaerobic codigestion
of Kimchi factory wastesilageandswinemanureunder
mesophilic conditions, Bioresouce Technology, 124,
2012, 489–494.
[14] O. W. Orhorhoro, E. K, Orhorhoro, P.O. Ebunilo, P.O.
Analysis of the effect of carbon/nitrogen(C/N)ratioon
the performance of biogas yields for non-uniform
multiple feed stock availability and composition in
Nigeria. International Journal of Innovative Science,
Engineering & Technology, 3(5), 2016, 119-126
[15] S. Sumardiono, I. Syaichurrozi, Budiyono1 and S. B.
Sasongko. The Effect of COD/N Ratios and pH Control
to Biogas Production from Vinasse. International
Journal of Biochemistry Research & Review 3(4): 401-
413, 2013
[16] E. K. Orhorhoro, P. O. B. Ebunilo, E. G. Sadjere.Design of
Bio-Waste Grinding Machine for Anaerobic Digestion
(AD) System. European Journal of Advances in
Engineering and Technology,4 (7), 2017, 560-568
[17] P. O. Ebunilo, S. A. Aliu, E. K. Orhorhoro. Performance
Study of a Biogas Pilot Plant using Domestic Wastes
from Benin Metropolis. International Journal of
Thermal & Environmental Engineering volume 10(2),
2015, 135-141

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Performance Evaluation of the Effect of pH and Temperature on the Biogas Yield of Co-Digestion of Pig Manure and Water Hyacinth

  • 1. International Journal of Trend in Scientific Research and Development (IJTSRD) Volume: 3 | Issue: 2 | Jan-Feb 2019 Available Online: www.ijtsrd.com e-ISSN: 2456 - 6470 @ IJTSRD | Unique Reference Paper ID – IJTSRD21410 | Volume – 3 | Issue – 2 | Jan-Feb 2019 Page: 455 Performance Evaluation of the Effect of pH and Temperature on the Biogas Yield of Co-Digestion of Pig Manure and Water Hyacinth Nse Peter Essang Department of Petroleum and Natural Gas Processing Engineering, Petroleum Training Institute, Effurun, Nigeria ABSTRACT In this research work, the effect of pH and temperature on the biogas yield of co-digestion of Pig manure and water hyacinth were investigated experimentally in laboratoryscale anaerobicbioreactors.Theco-digestionwasrun foraHydraulicRetention Time thirty six days. The volumetric yield of biogas was noted once there is biogas build up at regular intervals using water displacement method. A total of ten evacuations were made and the data obtained was used to evaluate the effect of the aforementioned anaerobic digestion parameters. The experimental results revealed that a neutral pH value of 7 yielded optimum biogas yields compared to a pH value above and below 7. Moreover, from all the experimental mesophilic temperature used in this research work, an optimum mesophilic temperature of 37 oC favoured the optimum biogas yield. KEYWORDS: pH, Biogas yield, Hydraulic retention time, Pig manure, Water Hyacinth, Optimum biogas yield 1. INTRODUCTION The increasing demand for energy,inadequateavailabilityof conventional energy supplied such as fossil and wood fuel resources, increase in crude oil prices, and the increasing concern for environmental issues have challenged researchers across the world to develop an alternative energy means that is clean and sustainable energy through the utilization of non-conventional renewable energy sources [1-4]. In this respect, biogas production from anaerobic digestion or co-digestionprocessof biodegradable organic waste will be a welcome development. The anaerobic digestion (AD) process has become an increasingly vital industrial process. The production of biogas from AD process is of growing interest across the world [5-7] and this is due to decline in wood and fossil fuel resources and their resulting effect on the ozone layer [8]. Worldwide greenhouse gas (GHG) emissions from biomass have doubled since the 1960s and could further increase by 30% if nothing is done about it. Anaerobic digestion is widely as a treatment option for the disposal of municipal solid waste on a par with the composting technologies. It mainly combines with the energy recovery benefits, greenhouse gas mitigation and produces stable end products, which can be furtherupgradedascompostforland use applications [9]. To optimize the rate of biogas yield, itis essentialtooptimize the process parameters involved in the digestion process. Many researchers investigated the effects of process parameters involved in the biogas production and reported their findings. Orhorhoro et al. [10] investigated the effect organic loading rate (OLR) on biogas yield from food waste, water hyacinth, and cow dung, waste water from abattoir, poultry dropping and pig dung. Their experiment was conducted within a mesophilic temperature range of 360C- 370C, percentage total solid (%TS) of 9.98% and percentage volatile solid (%VS) of 78%. pH meter was used to monitored the daily pH reading of the slurry. They reported that the quantity of biogas yieldfromthefeedstock increases with increasing organic load rate totheoptimum valueof 1.5 kg/m3 and started decreasing above theoptimum valuefora single stage AD reactor for a three-stages continuous AD reactors there was a continuousincreaseinbiogasyield with a successive increase in OLR from 1-5 kg/m3-3.0 kg/m3. Sivakumar et al. [11] investigated the effect of pH using spoiled milk as substrate and reported that the substrate with 7 pH resulted better biogas yield. Kafle et al [12] investigated the effect of co-digestion of Kimchi factory waste silage and swine manure under mesophilic temperature condition. The results suggested that Kimchi factory waste could be effectively treated by making silage, and the silage could be used as a potential co-substrate to enhance biogas production from swine manure digester. Deepanraj et al. [13] studied the effect of temperature on biogas production using food waste in a lab scale batch reactor and found that the operating temperature of 50°C achieved maximum biogas yield. Orhorhoro et al. [14] analyzed of the effect of Carbon/Nitrogen (C/N) ratio on the performance of biogas yields for non-uniform multiple feed stock availability and composition in Nigeria. The results obtained from their research work show that C/N ratio of substrates affects hydraulic retention time, biogas yield and the rate of frequency of evacuation. Therefore, for a better biogas yield, combination of low and high C/N ratio substrates is recommended. Sumardiono et al. [15] investigated the effect of COD/N ratios of substrate and pH control to biogas production from vinasse. Their study used anaerobic digestion-laboratoryscaleatroomtemperaturein batch system. Urea was added as nitrogen source to adjust COD/N ratios of 400/7, 500/7, 600/7, and 700/7. Initial pH for all variables was adjusted 7.0 by using NaOH solution. The results obtained reveal that biogas formed at COD/N ratio of control variable (1436/7); 400/7; 500/7; 600/7; 700/7 were 3.673; 4.909; 6.079; 6.096; 5.631 mL/g COD respectively. pH profiles for all variables were decreasing from beginning until endingof fermentation. With controlled pH, pH of substrates was maintained at neutral condition,so methanogenic bacteria could grow well in the digesters. Consequently biogas formed at controlled pH was larger
  • 2. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Reference Paper ID – IJTSRD21410 | Volume – 3 | Issue – 2 | Jan-Feb 2019 Page: 456 than that at uncontrolled pH. The values of COD removal for COD/N ratio of control variable; 400/7; 500/7; 600/7; 700/7 were 1.27±0.43; 1.59±0.43; 2.85±0.39; 3.21±0.49; 2.22±0.39 % respectively at uncontrolled pH, whereas at controlled pH the values of these were 11.98±0.56; 12.82±0.56; 12.03±0.94; 13.05±0.35; 12.61±0.56 % respectively. However, enough research works were not reported on biogas yield performance of co-digestion of animal manure and seed weeds, thus this research work. 2. Materials and Methods Water hyacinth used in this research work was harvested from River Ethiope, Boboroku- Jesse, Nigeria (Figure 1), and the Pig manure collected from Pig farm, Jesse, Nigeria (Figure 2). The experiment was carried out in laboratory- scale reactors as depicted in the schematic diagram (Figure 3). The volume of each reactor was 2,000 ml with a working volume of 1250 ml. All the reactors were purged with nitrogen before start-up in order to create anaerobic condition. The mixing was continuous and thiswasachieved using magnetic stirrer. The experiment was subjected to mesophilic temperature range of 36 0C as recommended by Ebunilo et al. [2]. A pH meter wasmonitoredusingelectronic pH metering (Figure 4). Figure 1: Water Hyacinth Figure 2: Pig Manure Figure 3: Experimental Setup Figure 4: pH Meter 3. Results and Discussion The roots of the water hyacinth were gently detached and the remaining parts properly washed and grinded using a grinding machine. The grinded water hyacinth was co- digested with the Pig manure to form slurry. According to Orhorhoro et al., [16], grinding increased the surface area of contact for the microbial activity, so that biogas yield would start within the shortest possible time. Preparation of fermentation of slurry was by addition and vigorous mixing of total substrate with an equivalent amount of water needed for maximum yield. The ratio of total substrate to water was 1:2 as recommended by Ebunilo et al., [17]. The amount of biogas yield was measured once there is an indication of biogas build up in the measuring cylinder. The measuring cylinder was then inverted with the gas pressure displacing equal amount of water and the readings were recorded. This procedure was repeated ten (10) times to ascertain the total volume of biogas produced. A pH meter was used to monitor the pH of the system. To measure the pH of the slurry, the probe (glass electrode) was inserted into the sample of the slurry after each evacuation. The results obtained show that optimum biogas yield was obtained at pH neutral reading of 7. Furthermore, a pH values below and above the optimum biogas yielding pH value of 7 brings about drops in biogas yield. Figure 5: Results of Performance Evaluation
  • 3. International Journal of Trend in Scientific Research and Development (IJTSRD) @ www.ijtsrd.com eISSN: 2456-6470 @ IJTSRD | Unique Reference Paper ID – IJTSRD21410 | Volume – 3 | Issue – 2 | Jan-Feb 2019 Page: 457 It was also observed that temperature affect the biogas yield throughout the hydraulic retention time. Anoptimumbiogas yields was obtained at optimum mesophilic temperature of 37 oC, and this agree with the research work of Ebunilo et al. [2]. 4. Conclusion In this research work, the effect of pH and temperature on biogas yield from co-digestion of Pig manure and water hyacinth were successfully evaluated The results obtained from the research work show that an optimum biogas yield is favored with a slurry pH of neutralityvalueof7.Moreover, for an optimum biogas yield, an optimum mesophilic temperature is required. Besides, the abundant water hyacinth in River Ethiope and Pig manure in Jesse can be used for production of biogas which can be used in place of conventional energy such as wood and fossil fuel. References [1] E. K. Orhorhoro, P. O. Ebunilo, E. G. Sadjere. Development of a Predictive Model for Biogas Yield Using Artificial Neural Networks (ANNs) Approach. American Journal of Energy and Power Engineering, 2017; 4(6): 71-77 [2] P. O. Ebunilo, E. K. Orhorhoro, V. Oboh, P. U. Onochie. Effect of Temperature on Biogas Yields Using South- South Nigeria as a Case Study. International Journal of Technology Enhancements and Emerging Engineering Research, 2016, 4(3), pp. 50-54 [3] E. K. Orhorhoro, O. W. Orhorhoro, A. E. Ikpe. A Study of Solar Energy Potential in Sapele, Nigeria. Int. J. of Thermal & Environmental Engineering, 13(2), 2016, 129-133 [4] G. K. Kafle, S. Bhattarai, S.H. Kim, L. Chen, Anaerobic digestion of Chinese cabbage waste silage with swine manure for biogas production: batch and continuous study, Environmental Technology, 35, 2014, 2708– 2717. [5] E. K. Orhorhoro, P. O. Ebunilo, E. G. Sadjere. Experimental Determination of Effect of Total Solid (TS) and Volatile Solid (VS) on Biogas Yield. American Journal of Modern Energy, 2017, 3(6): 131-135 [6] W. Qiao, X. Yan, J. Ye, Y. Sun, W. Wang, Z. Zhang. Evaluation of biogas productio from different biomass wastes with/without hydrothermal pretreatment. Renewable Energy, 36, 2011, 3313-3318 [7] T. Subramani, M. Nallathambi. Mathematical Model for Commercial Production of Bio-Gas fromSewageWater and Kitchen Waste. International Journal of Modern Engineering Research (IJMER), 2 (4),2012,1588-1595 [8] P. O. Osunde, P. O. B Ebunilo, E. K. Orhorhoro. Preliminary Evaluation of a Biogas Purification Filter Suitable for use in Nigeria Journal of Scientific and Engineering Research, 2017, 4(10), 125-134 [9] E. Dogan, G.N. Demirer, Biogas generation by two- phase anaerobic digestion of organic fraction of municipal solid waste, Journal of Renewable & Sustainable Energy, 4, 2012, 063131 [10] E. K. Orhorhoro, P.O. Ebunilo, E. G. Sadjere. Effect of Organic Loading Rate (OLR) on Biogas Yield Using a Single and Three-Stages Continuous Anaerobic Digestion Reactors. International Journal of Engineering Research in Africa, Vol. 39, pp. 147-155 [11] H. Raheman, S. Mondal, Biogas production potential of jatropha seed cake, Biomass and Bioenergy, 37, 2012, pp.25-30. [12] P. Sivakumar, M. Bhagiyalakshmi, and K. Anbarasu, Anaerobic treatment of spoiled milk from milk processing industryforenergyrecovery—A laboratory to pilot scale study, Fuel, 96, 2012, 482–486. [13] G. K. Kafle, S.H. Kim, Sung, Batch anaerobic codigestion of Kimchi factory wastesilageandswinemanureunder mesophilic conditions, Bioresouce Technology, 124, 2012, 489–494. [14] O. W. Orhorhoro, E. K, Orhorhoro, P.O. Ebunilo, P.O. Analysis of the effect of carbon/nitrogen(C/N)ratioon the performance of biogas yields for non-uniform multiple feed stock availability and composition in Nigeria. International Journal of Innovative Science, Engineering & Technology, 3(5), 2016, 119-126 [15] S. Sumardiono, I. Syaichurrozi, Budiyono1 and S. B. Sasongko. The Effect of COD/N Ratios and pH Control to Biogas Production from Vinasse. International Journal of Biochemistry Research & Review 3(4): 401- 413, 2013 [16] E. K. Orhorhoro, P. O. B. Ebunilo, E. G. Sadjere.Design of Bio-Waste Grinding Machine for Anaerobic Digestion (AD) System. European Journal of Advances in Engineering and Technology,4 (7), 2017, 560-568 [17] P. O. Ebunilo, S. A. Aliu, E. K. Orhorhoro. Performance Study of a Biogas Pilot Plant using Domestic Wastes from Benin Metropolis. International Journal of Thermal & Environmental Engineering volume 10(2), 2015, 135-141