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IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 210
ASSESSMENT OF COMPOSTING, ENERGY AND GAS GENERATION
POTENTIAL FOR MSW AT ALLAHABAD CITY IN INDIA
Sumedha Chakma1
, Rakesh Chandra Vaishya2
1
Assistant Professor, 2
Professor, Civil Engineering Department, Motilal Nehru National Institute of Technology
Allahabad, Uttar Pradesh, India, s_chakma@rediffmail.com, chakma@mnnit.ac.in, rcvaishya@mnnit.ac.in
Abstract
Management of municipal solid waste (MSW) is a major concerned for Allahabad city as the city is growing with population and the
increase is 20.74 percent for the last 10 years. In this regard, MSW samples were collected from twenty wards and three dumpsites to
estimate composting, energy and gas generation potential for MSW Management. It was observed that the MSW is not suitable for
composting because C/N ratio was found to be less than 30:1. Existing gas generation model is modified and found a bioreactor
landfill with leachate recirculation would be the best method for the MSW management.
Keywords: Municipal solid waste, Energy, Composting, Gas generation, Calorific Value, landfill
-----------------------------------------------------------------------***-----------------------------------------------------------------------
1. INTRODUCTION
Waste disposal in open area or low lying area are being
practised by communities for more than five thousand years
[18]. Many Indian cities still considered open dumping as the
preferred means of disposing municipal solid waste (MSW)
because it is generally the easiest and the cheapest way of
dealing the refuse compared to other methods like incineration
and composting. But due to urbanization and increase in
population from 11% in 1901 to 26% in 2001 [8], the cities are
facing serious problems of managing its MSW. Although in
India, MSW (Management & Handling) Rules has come into
effect in the year 2000 for collection, segregation, storage,
transportation, processing and disposal of municipal solid.
However, this rules are not being fully implemented at
Allahabad city and disposal of MSW is still continues through
open dumping [11]. This practice is not only causes an
environmental hazard but also an ecological imbalance that
leads to land, water and air pollution [12]. The major affects
that takes place in and around the dumping sites are methane
emission, greenhouse effects, ozone depletion, odours,
generation of leachate, settlement due to biodegradation and
water pollution [5; 6; 7].
The production of MSW was 509 ton/day with per capita
generation rate 0.52 kg in 2005 for Allahabad city and
expected to reach the generate rate 0.60 kg/capita/day in 2012
[15; 16]. MSW of the city contains 45.3% organic matter and
40% inert materials (bricks, fine dust, rubber, wood, leather,
etc.). The percentage of recyclable materials (glass, paper
plastics, metals etc.) is very low. It is due to rag pickers, who
collect and segregate recyclable materials from collection
point and disposal sites which are not in big numbers [16].
There is no modern landfill available to manage the MSW and
the waste is dumped in a mixed form on open waste land or
low lying areas. These days, the most promising technologies
for the MSW management are composting, incineration and
landfilling. Composting of MSW is the most simple and cost
effective technology for treating the organic fraction of MSW
which can be determined from C/N ratio. Incineration is an
efficient way to reduce the waste volume but required heavy
investments with high operating costs and suitability can be
determined from the calorific value of the MSW. Modern
landfilling with leachate recirculation and energy recovery
such as bioreactor landfill has also proved good result for
MSW management [14].
In the present study various physico-chemical parameters like
Carbon, Hydrogen, Oxygen, Nitrogen, Sulphur, along with
moisture content and volatile matter (VM) for MSW were
analyzed and determined the energy, composting and gas
generation potential for the Allahabad city. The outcomes of
the analysis were used to suggest the best suitable method of
MSW management among energy recovery, composting and
landfilling.
2. STUDY AREA
2.1 Study area
Allahabad, a major city of east Uttar Pradesh State (India),
situated at 25.25 North latitude and 81.58 East longitudes. The
population was 49, 36, 105 in 2001 and has reached to 59, 59,
798 in 2011 [10]. This shows that city is growing with
population and there is an increase in 20.74 percent since 2001.
The total area under Allahabad district is about 5481 Sq km.
Allahabad Municipal Corporation is responsible for the
management of the MSW generated in the city. The city is
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 211
having 80 wards divided into four zones (N, S, E, and W) and
six dumpsites. Out of 80 wards and six dumpsites, 20 wards
and 3 dumpsites were selected for sample collection as shown
in Figure 1. Samplings were carried out during the months of
July, 2009 to June 2010 as per international standard [3]. Total
five numbers of sampling were carried out during the mention
period with equal interval of time. The selection of the source
of MSW was predetermined randomly to accommodate all
types of sources (i.e. high, medium and low residential
households, institutional, commercial and other sources). To
carry out the analysis a number of items of equipment like
hand protective plastic gloves for handling, scales capable of
weighing up to 10kg, smaller range scales for detailed analysis,
10 mm thick plastic sheets to cover the floor, plastic bag for
collection and sorting of solid wastes, trash bag for collection
of already processed wastes, and field observation were used.
2.2. MSW sample preparation
Samples collected from different locations were
heterogeneous mixtures. The collected samples were
segregated on the basis of visual inspection. One of the
fractions obtained in the segregation process was a mixture of
kitchen/ food waste, plants, and other biodegradable matter
referred as compostable matter in this study. The portions of
the waste were not taken for the analysis includes metals, glass,
rubber, plastics, bones, textiles etc. Polythene bags were used
for the collection of wastes. Polythene bags were made air
tight to prevent the moisture losses.
Figure1. MSW Sampling Site
The collected samples were transferred to the laboratory on
the day of sampling. It is not possible to remove all the
unwanted substances (metals, glass, plastics etc) from the
sample on the spot therefore the sample was re-segregated in
to the laboratory to remove these substances. To prepare
homogeneous mixture of the MSW, samples were then
properly mixed with the help of mixer. A properly mixed
sample from mixer of 50 g was taken and oven dried in a
constant temperature of 105 °C for an hour. Grinding of oven
dried samples was done with the help of small size mixer to
convert it in the powdered form.
3. METHODOLOGY
3.1 Energy Content
The chemical compositions of the organic matter in MSW
such as the percentage of the C , H, O, N and S were
determine by using CHNS analyzer (Model-Elementary Vario
MICRO) as per ASTM E 777-87 & ASTM778-87 [3].
Calorific value of the MSW was then determined by using
Mott and Spooner Model shown [13] as,
Energy Content (kcal/kg)
=80.3C + 338.9H - 3.47O + 22.49S (1)
Where C = Carbon in Percent, H = Hydrogen in Percent, O =
Oxygen in Percent, S = Sulfur Percent
Again, on the basis of volatile organic matter (VM) and
moisture content (W) the energy content can be obtained by
Bento’s model [1] as
Energy Content (kcal/kg)
= 44.75VM - 5.85W + 21.2 (2)
3.2 Gas generation
Landfill gas generation can be modelled using first order
kinetic empirical model to estimate methane gas [2; 17] by Eq.
3.
)exp(0 ktWkLG  (3)
Where, G is the rate of methane generation (m3
/year), W is
mass of solid waste deposited (ton/year), Lo is the methane
generation potential (m3
/ton), and k is the first order kinetic
decay constant (1/year), t is time interested for gas generation
(year).
US EPA Land GEM model [17] is modified incorporating gas
generation with depth (z) as shown in Eq. (4).
 

n
i
z
j
ijj ktkLWG
1 1
,0 )exp( (4)
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 212
where, j is the starting time period of waste disposal, z is the
total number of years for waste disposal (year) with depth, i is
the post closure landfill starting period, n is the post closure
gas generation period, Wj is mass of solid waste deposited
(ton/year), , and k is the first order kinetic decay constant
(1/year).
4. RESULTS AND ANALYSIS
The moisture content in the MSW varies maximum amongst
all the compositions ranging from 21.3% to 39.08% with an
average percentage 27.33% as depicted in Table 1. It was
observed that the dumpsites and the sites having low
collection frequency generally have lower value of the
moisture content. The moisture content of the waste collected
from commercial areas were observed higher value since
regular collection of waste takes place from these areas and
also the waste contains high amount of food waste. Similarly,
Oxygen content varies from 12.22 to 22.25% and Carbon
varies from 7.33% to 13.74% with an average value 12.34 %.
Solid waste contains less percentage of Hydrogen, Nitrogen
and Sulphur and estimated value is less than 1% for Nitrogen
and sulphur; however hydrogen varies from 0.81 to 1.60 with
an average value 1.33% as shown in Table 1.
4.1 C/N Ratio
The carbon to nitrogen ratio (C: N ratio) is the relative
percentage of carbon to that of nitrogen in various organic
materials. C/N ratio is a critical parameter in the design of
composting system and should ideally lie between 25 and 50,
the optimum value being 25:1 [4]. In present study it was
observed that the C/N ratio of wastes is not very high. C/N
ratio in the MSW varies from 16.00 to 24.55% as depicted in
Figure 2 with an average percentage 19.72%. The C/N ratio
can be adjusted by blending of waste of high C/N ratio (e.g.
saw dust, paper) with the waste of low C/N ratio (e.g. yard
waste, raw activated sludge).
0
5
10
15
20
25
30
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23
All Sites
C/NRatio
Figure 2 C/N Ratio for all sites
4.2 Energy content
The percentage of calorific value present for all the sites is
shown in Figure 3. The calorific value of the waste is not very
high because of lower percentage of the carbon and higher
oxygen content in the waste. It was estimated energy content
varies in the range of 2495.60 to 2972.02 kcal/kg using Eq. (1);
however, Eq.(2) estimated using volatile organic content and
moisture content lesser energy content and average value was
observed as 811.05 kcal/kg. This shows that MSW is not
suitable for incineration as minimum recommended value for
incineration is 1433 kcal/kg for any season [19]. However
with dried condition, it is possible to use for Incineration.
0
500
1000
1500
2000
2500
3000
3500
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23
All Sites
EnergyContent(kcal/kg)
Bento Model
Mott and Spooner Model
Figure 3 Energy content for all sites
4.3 Gas generation
It is assumed twenty years for the closure of the landfill with
all the waste generated dumped in landfills. The management
of solid waste for Indian condition suggested that it can be
made controlled sanitary landfill or bioreactor landfills [14].
The model parameter Lo is taken as 170 m3
/ton and k as 0.05
year-1
for controlled sanitary landfill while 0.15 for bioreactor
landfill with leachate recirculation respectively [9]. W was
calculated 16.33 ton/year for the Allahabad city. Methane
production rates estimated using Eq. (2) is shown in Figure 4
for controlled and bioreactor landfill with leachate
recirculation. It depicts that the gas generation is higher at the
initial and during closure of landfill i.e. at the end of 20 years
for bioreactor landfills with leachate recirculation compared to
controlled sanitary landfills. After 40 years of the closure of
landfills, there would be no gas generation for bioreactor
landfills whereas gas generation would continue beyond 90
years for controlled sanitary landfills. This shows that
bioreactor landfills with leachate recirculation would be
beneficial for Allahabad city because it will not only generate
energy but also possible to use landfill after 30 to 40 years of
closure.
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 213
Table 1: Measured values of C, H, N, S, O, VM and W (% dry weight)
Site No. C H N S O VM W
1 9.22 0.95 0.56 0.20 36.10 15.64 29.09
2 10.25 1.08 0.48 0.21 35.18 15.47 29.33
3 7.33 0.81 0.46 0.19 31.82 14.65 24.09
4 12.95 1.50 0.65 0.23 43.34 20.49 35.20
5 9.55 1.07 0.54 0.19 44.66 16.97 36.42
6 13.74 1.60 0.69 0.18 43.96 22.18 34.68
7 12.67 1.25 0.52 0.21 43.03 19.33 35.46
8 10.97 1.23 0.62 0.19 43.97 17.79 36.39
9 11.78 1.28 0.65 0.20 35.42 18.37 28.44
10 11.19 1.28 0.61 0.18 42.68 18.53 34.63
11 11.31 1.23 0.57 0.20 43.72 18.71 35.37
12 11.26 1.26 0.57 0.21 36.65 19.27 27.54
13 9.65 1.15 0.50 0.20 42.05 15.97 35.03
14 7.68 0.96 0.45 0.20 32.65 13.20 26.60
15 11.63 1.38 0.56 0.25 31.86 18.36 24.57
16 11.34 1.23 0.62 0.20 41.38 18.02 33.96
17 10.25 1.19 0.43 0.19 30.83 18.12 22.82
18 12.23 1.44 0.62 0.23 45.30 18.07 39.08
19 10.53 1.16 0.53 0.18 29.47 16.82 22.54
20 12.93 1.55 0.70 0.26 34.94 20.82 26.68
21 10.55 1.22 0.54 0.24 29.92 18.33 21.30
22 13.47 1.34 0.58 0.20 41.92 22.25 32.08
23 13.19 1.40 0.56 0.22 36.47 21.37 27.71
AVG 11.12 1.24 0.57 0.21 38.14 18.21 30.39
CONCLUSIONS
Energy, composting and gas generation potential were studied
to suggest the best sustainable method for MSW management.
It was observed that MSW for Allahabad city is not suitable
for composting because of low C/N ratio. However, it is
possible to accomplish incineration in dried form and adding
high calorific value material such as plastic. The present
scenario suggested that best suitable technique for the
sustainable MSW management would be bioreactor landfill
with leachate recirculation. Further research can be done to
suggest best composting methods by the process of
segregation and blending of waste.
0
500
1000
1500
2000
2500
3000
0 10 20 30 40 50 60 70 80 90 100
Year
CH4Production(m3
/year)
0.05
0.15
Figure 4 Estimated Methane productions
ACKNOWLEDGEMENTS
The author is acknowledged Mr. Alok Kumar Yadav for
conducting the experiment.
REFERENCES
[1] Abu-Quadais, M., Abu-Qdais, H. A. (2000) Energy
content of municipal solid waste in Jordan and its
potential utilization. Energy Conversion and
Management, 41, 983-991.
[2] Amini H. R.,Reinhart D. R. and Mackie K. R. (2012).
Determination of first-order landfill gas modeling
parameters and uncertainties. Waste Management 32,
305–316.
[3] ASTM D 4687-95(2006) & ASTM D 5231-92(2003),
ASTM International, United State.
[4] Central Public Health and Environmental Engineering
Organisation (CPHEEO), (2000). Manual on Municipal
Solid Waste Management. Ministry of Urban
Development, Govt. of India.
[5] Chakma, S. and Mathur, S (2007)a. Leachate: A threat
to groundwater contamination at Delhi. International
Conference on Water Resource Management:
Challenges and Opportunities in the 21st
Century,
Silchar, Assam, April 23-25.
IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308
__________________________________________________________________________________________
Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 214
[6] Chakma, S. and Mathur, S (2007)b. Modelling gas
generation from landfills. Environmental Awareness
and Management, 137-142.
[7] Chakma, S. and Mathur, S. (2012). “Post closure long-
term settlement for MSW landfills.” Journal of
Hazardous, Toxic, and Radioactive Waste, ASCE
Publication 17(2), 81-88.
[8] Ghose, M. K., Dikshit, A. K., and Sharma, S. K. (2006).
A GIS based transportation model for solid waste
disposal – A case study on Asansol municipality. Waste
Management, 26(11), 1287-1293.
[9] Hossain M.S., Gabr M. A., and Barlaz,M. A. (2003).
Relationship of Compressibility Parameters to
Municipal Solid Waste Decomposition. Journal of
Geotechnical and Geoenvironmental Engineering 129,
1151–1158.
[10] http://www.census2011.co.in/census/district/546-
allahabad.html.
[11] http://www.cpcb.nic.in/Municipal_Solid_Waste.php
[12] Kansal, A., Prasad, R. K., and Gupta, S. (1998). Delhi
municipal solid waste and environment – an appraisal.
Indian Journal of Environment Protection 18(2), 123-
128.
[13] Kathiravale, S., Yunus, M., Sopiahk N., Samsuddin, A.
H. 2003. Energy Potential from municipal solid waste
in Malaysia. Journal of Renewable Energy, 29, 559-567.
[14] Mathur, S. and Chakma, S. (2003). MSW Management
through Bioreactor Landfill”, Proc. on Advances in
Civil Engineering: Perspectives of Developing
Countries, HBTI, Kanpur, Vol.2, 546-552.
[15] NEERI Report. (2005). Assessment of status of
municipal solid waste management in metro cities, state
capitals, class I cities and class II towns. National
Environmental Engineering Research Institute, Nagpur.
[16] Sharholy, M., Ahmad, K., Vaishya, R.C., and
Gupta, R.D. (2007). Municipal solid waste
characteristics and management in Allahabad.
Waste Management, 27, 490–496.
[17] U.S. Environmental Protection Agency (US EPA).
(1998). User’s manual lanfill gas emissions: Model
version 2.0. EPA/600/R-98/054, Research Triangle
Park, N.C.
[18] White-Hunt., K. (1980). Domestic Refuse - A brief
History. Solid Waste, 70, 609.
[19] World Bank (1999). Technical Guidance Report on
Municipal Solid Waste Incineration. The World Bank
Washington, DC.
BIOGRAPHIES
Dr. Sumedha Chakma did his Ph.D. from
Indian Institute of Technology Delhi. His
research fields are solid waste management,
settlement in landfills, bioreactor landfills,
and infiltration studies. He has more than
25 research publications.
Dr. Rakesh Chandra Vaishya did his
Ph.D. from Indian Institute of Technology
Bombay. His research fields are solid
waste management, air pollution,
environmental impact assessment, and
rural water supply. He has more than 50
research publications.

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Assessment of composting, energy and gas generation potential for msw at allahabad city in india

  • 1. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 210 ASSESSMENT OF COMPOSTING, ENERGY AND GAS GENERATION POTENTIAL FOR MSW AT ALLAHABAD CITY IN INDIA Sumedha Chakma1 , Rakesh Chandra Vaishya2 1 Assistant Professor, 2 Professor, Civil Engineering Department, Motilal Nehru National Institute of Technology Allahabad, Uttar Pradesh, India, s_chakma@rediffmail.com, chakma@mnnit.ac.in, rcvaishya@mnnit.ac.in Abstract Management of municipal solid waste (MSW) is a major concerned for Allahabad city as the city is growing with population and the increase is 20.74 percent for the last 10 years. In this regard, MSW samples were collected from twenty wards and three dumpsites to estimate composting, energy and gas generation potential for MSW Management. It was observed that the MSW is not suitable for composting because C/N ratio was found to be less than 30:1. Existing gas generation model is modified and found a bioreactor landfill with leachate recirculation would be the best method for the MSW management. Keywords: Municipal solid waste, Energy, Composting, Gas generation, Calorific Value, landfill -----------------------------------------------------------------------***----------------------------------------------------------------------- 1. INTRODUCTION Waste disposal in open area or low lying area are being practised by communities for more than five thousand years [18]. Many Indian cities still considered open dumping as the preferred means of disposing municipal solid waste (MSW) because it is generally the easiest and the cheapest way of dealing the refuse compared to other methods like incineration and composting. But due to urbanization and increase in population from 11% in 1901 to 26% in 2001 [8], the cities are facing serious problems of managing its MSW. Although in India, MSW (Management & Handling) Rules has come into effect in the year 2000 for collection, segregation, storage, transportation, processing and disposal of municipal solid. However, this rules are not being fully implemented at Allahabad city and disposal of MSW is still continues through open dumping [11]. This practice is not only causes an environmental hazard but also an ecological imbalance that leads to land, water and air pollution [12]. The major affects that takes place in and around the dumping sites are methane emission, greenhouse effects, ozone depletion, odours, generation of leachate, settlement due to biodegradation and water pollution [5; 6; 7]. The production of MSW was 509 ton/day with per capita generation rate 0.52 kg in 2005 for Allahabad city and expected to reach the generate rate 0.60 kg/capita/day in 2012 [15; 16]. MSW of the city contains 45.3% organic matter and 40% inert materials (bricks, fine dust, rubber, wood, leather, etc.). The percentage of recyclable materials (glass, paper plastics, metals etc.) is very low. It is due to rag pickers, who collect and segregate recyclable materials from collection point and disposal sites which are not in big numbers [16]. There is no modern landfill available to manage the MSW and the waste is dumped in a mixed form on open waste land or low lying areas. These days, the most promising technologies for the MSW management are composting, incineration and landfilling. Composting of MSW is the most simple and cost effective technology for treating the organic fraction of MSW which can be determined from C/N ratio. Incineration is an efficient way to reduce the waste volume but required heavy investments with high operating costs and suitability can be determined from the calorific value of the MSW. Modern landfilling with leachate recirculation and energy recovery such as bioreactor landfill has also proved good result for MSW management [14]. In the present study various physico-chemical parameters like Carbon, Hydrogen, Oxygen, Nitrogen, Sulphur, along with moisture content and volatile matter (VM) for MSW were analyzed and determined the energy, composting and gas generation potential for the Allahabad city. The outcomes of the analysis were used to suggest the best suitable method of MSW management among energy recovery, composting and landfilling. 2. STUDY AREA 2.1 Study area Allahabad, a major city of east Uttar Pradesh State (India), situated at 25.25 North latitude and 81.58 East longitudes. The population was 49, 36, 105 in 2001 and has reached to 59, 59, 798 in 2011 [10]. This shows that city is growing with population and there is an increase in 20.74 percent since 2001. The total area under Allahabad district is about 5481 Sq km. Allahabad Municipal Corporation is responsible for the management of the MSW generated in the city. The city is
  • 2. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 211 having 80 wards divided into four zones (N, S, E, and W) and six dumpsites. Out of 80 wards and six dumpsites, 20 wards and 3 dumpsites were selected for sample collection as shown in Figure 1. Samplings were carried out during the months of July, 2009 to June 2010 as per international standard [3]. Total five numbers of sampling were carried out during the mention period with equal interval of time. The selection of the source of MSW was predetermined randomly to accommodate all types of sources (i.e. high, medium and low residential households, institutional, commercial and other sources). To carry out the analysis a number of items of equipment like hand protective plastic gloves for handling, scales capable of weighing up to 10kg, smaller range scales for detailed analysis, 10 mm thick plastic sheets to cover the floor, plastic bag for collection and sorting of solid wastes, trash bag for collection of already processed wastes, and field observation were used. 2.2. MSW sample preparation Samples collected from different locations were heterogeneous mixtures. The collected samples were segregated on the basis of visual inspection. One of the fractions obtained in the segregation process was a mixture of kitchen/ food waste, plants, and other biodegradable matter referred as compostable matter in this study. The portions of the waste were not taken for the analysis includes metals, glass, rubber, plastics, bones, textiles etc. Polythene bags were used for the collection of wastes. Polythene bags were made air tight to prevent the moisture losses. Figure1. MSW Sampling Site The collected samples were transferred to the laboratory on the day of sampling. It is not possible to remove all the unwanted substances (metals, glass, plastics etc) from the sample on the spot therefore the sample was re-segregated in to the laboratory to remove these substances. To prepare homogeneous mixture of the MSW, samples were then properly mixed with the help of mixer. A properly mixed sample from mixer of 50 g was taken and oven dried in a constant temperature of 105 °C for an hour. Grinding of oven dried samples was done with the help of small size mixer to convert it in the powdered form. 3. METHODOLOGY 3.1 Energy Content The chemical compositions of the organic matter in MSW such as the percentage of the C , H, O, N and S were determine by using CHNS analyzer (Model-Elementary Vario MICRO) as per ASTM E 777-87 & ASTM778-87 [3]. Calorific value of the MSW was then determined by using Mott and Spooner Model shown [13] as, Energy Content (kcal/kg) =80.3C + 338.9H - 3.47O + 22.49S (1) Where C = Carbon in Percent, H = Hydrogen in Percent, O = Oxygen in Percent, S = Sulfur Percent Again, on the basis of volatile organic matter (VM) and moisture content (W) the energy content can be obtained by Bento’s model [1] as Energy Content (kcal/kg) = 44.75VM - 5.85W + 21.2 (2) 3.2 Gas generation Landfill gas generation can be modelled using first order kinetic empirical model to estimate methane gas [2; 17] by Eq. 3. )exp(0 ktWkLG  (3) Where, G is the rate of methane generation (m3 /year), W is mass of solid waste deposited (ton/year), Lo is the methane generation potential (m3 /ton), and k is the first order kinetic decay constant (1/year), t is time interested for gas generation (year). US EPA Land GEM model [17] is modified incorporating gas generation with depth (z) as shown in Eq. (4).    n i z j ijj ktkLWG 1 1 ,0 )exp( (4)
  • 3. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 212 where, j is the starting time period of waste disposal, z is the total number of years for waste disposal (year) with depth, i is the post closure landfill starting period, n is the post closure gas generation period, Wj is mass of solid waste deposited (ton/year), , and k is the first order kinetic decay constant (1/year). 4. RESULTS AND ANALYSIS The moisture content in the MSW varies maximum amongst all the compositions ranging from 21.3% to 39.08% with an average percentage 27.33% as depicted in Table 1. It was observed that the dumpsites and the sites having low collection frequency generally have lower value of the moisture content. The moisture content of the waste collected from commercial areas were observed higher value since regular collection of waste takes place from these areas and also the waste contains high amount of food waste. Similarly, Oxygen content varies from 12.22 to 22.25% and Carbon varies from 7.33% to 13.74% with an average value 12.34 %. Solid waste contains less percentage of Hydrogen, Nitrogen and Sulphur and estimated value is less than 1% for Nitrogen and sulphur; however hydrogen varies from 0.81 to 1.60 with an average value 1.33% as shown in Table 1. 4.1 C/N Ratio The carbon to nitrogen ratio (C: N ratio) is the relative percentage of carbon to that of nitrogen in various organic materials. C/N ratio is a critical parameter in the design of composting system and should ideally lie between 25 and 50, the optimum value being 25:1 [4]. In present study it was observed that the C/N ratio of wastes is not very high. C/N ratio in the MSW varies from 16.00 to 24.55% as depicted in Figure 2 with an average percentage 19.72%. The C/N ratio can be adjusted by blending of waste of high C/N ratio (e.g. saw dust, paper) with the waste of low C/N ratio (e.g. yard waste, raw activated sludge). 0 5 10 15 20 25 30 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 All Sites C/NRatio Figure 2 C/N Ratio for all sites 4.2 Energy content The percentage of calorific value present for all the sites is shown in Figure 3. The calorific value of the waste is not very high because of lower percentage of the carbon and higher oxygen content in the waste. It was estimated energy content varies in the range of 2495.60 to 2972.02 kcal/kg using Eq. (1); however, Eq.(2) estimated using volatile organic content and moisture content lesser energy content and average value was observed as 811.05 kcal/kg. This shows that MSW is not suitable for incineration as minimum recommended value for incineration is 1433 kcal/kg for any season [19]. However with dried condition, it is possible to use for Incineration. 0 500 1000 1500 2000 2500 3000 3500 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 All Sites EnergyContent(kcal/kg) Bento Model Mott and Spooner Model Figure 3 Energy content for all sites 4.3 Gas generation It is assumed twenty years for the closure of the landfill with all the waste generated dumped in landfills. The management of solid waste for Indian condition suggested that it can be made controlled sanitary landfill or bioreactor landfills [14]. The model parameter Lo is taken as 170 m3 /ton and k as 0.05 year-1 for controlled sanitary landfill while 0.15 for bioreactor landfill with leachate recirculation respectively [9]. W was calculated 16.33 ton/year for the Allahabad city. Methane production rates estimated using Eq. (2) is shown in Figure 4 for controlled and bioreactor landfill with leachate recirculation. It depicts that the gas generation is higher at the initial and during closure of landfill i.e. at the end of 20 years for bioreactor landfills with leachate recirculation compared to controlled sanitary landfills. After 40 years of the closure of landfills, there would be no gas generation for bioreactor landfills whereas gas generation would continue beyond 90 years for controlled sanitary landfills. This shows that bioreactor landfills with leachate recirculation would be beneficial for Allahabad city because it will not only generate energy but also possible to use landfill after 30 to 40 years of closure.
  • 4. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 213 Table 1: Measured values of C, H, N, S, O, VM and W (% dry weight) Site No. C H N S O VM W 1 9.22 0.95 0.56 0.20 36.10 15.64 29.09 2 10.25 1.08 0.48 0.21 35.18 15.47 29.33 3 7.33 0.81 0.46 0.19 31.82 14.65 24.09 4 12.95 1.50 0.65 0.23 43.34 20.49 35.20 5 9.55 1.07 0.54 0.19 44.66 16.97 36.42 6 13.74 1.60 0.69 0.18 43.96 22.18 34.68 7 12.67 1.25 0.52 0.21 43.03 19.33 35.46 8 10.97 1.23 0.62 0.19 43.97 17.79 36.39 9 11.78 1.28 0.65 0.20 35.42 18.37 28.44 10 11.19 1.28 0.61 0.18 42.68 18.53 34.63 11 11.31 1.23 0.57 0.20 43.72 18.71 35.37 12 11.26 1.26 0.57 0.21 36.65 19.27 27.54 13 9.65 1.15 0.50 0.20 42.05 15.97 35.03 14 7.68 0.96 0.45 0.20 32.65 13.20 26.60 15 11.63 1.38 0.56 0.25 31.86 18.36 24.57 16 11.34 1.23 0.62 0.20 41.38 18.02 33.96 17 10.25 1.19 0.43 0.19 30.83 18.12 22.82 18 12.23 1.44 0.62 0.23 45.30 18.07 39.08 19 10.53 1.16 0.53 0.18 29.47 16.82 22.54 20 12.93 1.55 0.70 0.26 34.94 20.82 26.68 21 10.55 1.22 0.54 0.24 29.92 18.33 21.30 22 13.47 1.34 0.58 0.20 41.92 22.25 32.08 23 13.19 1.40 0.56 0.22 36.47 21.37 27.71 AVG 11.12 1.24 0.57 0.21 38.14 18.21 30.39 CONCLUSIONS Energy, composting and gas generation potential were studied to suggest the best sustainable method for MSW management. It was observed that MSW for Allahabad city is not suitable for composting because of low C/N ratio. However, it is possible to accomplish incineration in dried form and adding high calorific value material such as plastic. The present scenario suggested that best suitable technique for the sustainable MSW management would be bioreactor landfill with leachate recirculation. Further research can be done to suggest best composting methods by the process of segregation and blending of waste. 0 500 1000 1500 2000 2500 3000 0 10 20 30 40 50 60 70 80 90 100 Year CH4Production(m3 /year) 0.05 0.15 Figure 4 Estimated Methane productions ACKNOWLEDGEMENTS The author is acknowledged Mr. Alok Kumar Yadav for conducting the experiment. REFERENCES [1] Abu-Quadais, M., Abu-Qdais, H. A. (2000) Energy content of municipal solid waste in Jordan and its potential utilization. Energy Conversion and Management, 41, 983-991. [2] Amini H. R.,Reinhart D. R. and Mackie K. R. (2012). Determination of first-order landfill gas modeling parameters and uncertainties. Waste Management 32, 305–316. [3] ASTM D 4687-95(2006) & ASTM D 5231-92(2003), ASTM International, United State. [4] Central Public Health and Environmental Engineering Organisation (CPHEEO), (2000). Manual on Municipal Solid Waste Management. Ministry of Urban Development, Govt. of India. [5] Chakma, S. and Mathur, S (2007)a. Leachate: A threat to groundwater contamination at Delhi. International Conference on Water Resource Management: Challenges and Opportunities in the 21st Century, Silchar, Assam, April 23-25.
  • 5. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308 __________________________________________________________________________________________ Volume: 02 Issue: 08 | Aug-2013, Available @ http://www.ijret.org 214 [6] Chakma, S. and Mathur, S (2007)b. Modelling gas generation from landfills. Environmental Awareness and Management, 137-142. [7] Chakma, S. and Mathur, S. (2012). “Post closure long- term settlement for MSW landfills.” Journal of Hazardous, Toxic, and Radioactive Waste, ASCE Publication 17(2), 81-88. [8] Ghose, M. K., Dikshit, A. K., and Sharma, S. K. (2006). A GIS based transportation model for solid waste disposal – A case study on Asansol municipality. Waste Management, 26(11), 1287-1293. [9] Hossain M.S., Gabr M. A., and Barlaz,M. A. (2003). Relationship of Compressibility Parameters to Municipal Solid Waste Decomposition. Journal of Geotechnical and Geoenvironmental Engineering 129, 1151–1158. [10] http://www.census2011.co.in/census/district/546- allahabad.html. [11] http://www.cpcb.nic.in/Municipal_Solid_Waste.php [12] Kansal, A., Prasad, R. K., and Gupta, S. (1998). Delhi municipal solid waste and environment – an appraisal. Indian Journal of Environment Protection 18(2), 123- 128. [13] Kathiravale, S., Yunus, M., Sopiahk N., Samsuddin, A. H. 2003. Energy Potential from municipal solid waste in Malaysia. Journal of Renewable Energy, 29, 559-567. [14] Mathur, S. and Chakma, S. (2003). MSW Management through Bioreactor Landfill”, Proc. on Advances in Civil Engineering: Perspectives of Developing Countries, HBTI, Kanpur, Vol.2, 546-552. [15] NEERI Report. (2005). Assessment of status of municipal solid waste management in metro cities, state capitals, class I cities and class II towns. National Environmental Engineering Research Institute, Nagpur. [16] Sharholy, M., Ahmad, K., Vaishya, R.C., and Gupta, R.D. (2007). Municipal solid waste characteristics and management in Allahabad. Waste Management, 27, 490–496. [17] U.S. Environmental Protection Agency (US EPA). (1998). User’s manual lanfill gas emissions: Model version 2.0. EPA/600/R-98/054, Research Triangle Park, N.C. [18] White-Hunt., K. (1980). Domestic Refuse - A brief History. Solid Waste, 70, 609. [19] World Bank (1999). Technical Guidance Report on Municipal Solid Waste Incineration. The World Bank Washington, DC. BIOGRAPHIES Dr. Sumedha Chakma did his Ph.D. from Indian Institute of Technology Delhi. His research fields are solid waste management, settlement in landfills, bioreactor landfills, and infiltration studies. He has more than 25 research publications. Dr. Rakesh Chandra Vaishya did his Ph.D. from Indian Institute of Technology Bombay. His research fields are solid waste management, air pollution, environmental impact assessment, and rural water supply. He has more than 50 research publications.