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M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559
www.ijera.com 553 | P a g e
Studies On Development Of Fuel Briquettes Using Locally
Avaliable Waste
Ch. A. I. Raju, M. Satya, U. Praveena and K. Ramya Jyothi
Department of Chemical Engineering
Andhra University, Visakhapatnam – 530 003
ABSTRACT:
The Energy requirement is increasing day by day as the number of industries is increasing proportionately and
the present power supply is unable to meet the energy demand. To combat this energy shortage, developed as
well as developing countries are putting more efforts into R&D to tap alternative energy sources. State policies
are also being formulated to encourage alternative sources of energy. In India alone, it is proposed that 17,000
MW should be produced from biomass. Although other options like gasification can be used for power
generation, briquetting of biomass can be considered for its economics, reliability and ease of operation.
Briquettes of small size can be used in gasifies for power generation. If the plant sites are chosen properly for
easy availability of raw material, the agro-residues can be briquetted to reduce further transportation costs and
associated pollution. This also improves the handling characteristics of biomass. The briquettes so obtained are
very good fuels for local small scale industries and domestic purposes.
Key Words: Fuel Briquettes, Proximate Analysis, Ultimate Analysis, XRD, SEM
I. Material and methods:
Sugarcane waste: India, as we all know is
the second biggest sugarcane growing country in the
World, only behind Brazil. Every year, 4 million
hectares had been planted with sugarcane. Sugar
plant can process 40 million tons sugarcane every
year. For each tone of sugarcane crushed, about 300
kg of bagasse is retrieved. Previously bagasse is
used as the fuel of sugar production. However only
a third of bagasse are flamed, the remaining is
discarded. That is to say, making bagasse into
briquettes contains huge potential
Teak leaves: The primary benefit of leaf and yard
waste is the potential for immediate diversion of a
significant portion of the state's solid waste stream
from disposal facilities. The economic and
environmental benefits which result from
eliminating this material from disposal facilities and
converting it to briquettes have provided
municipalities with the incentive to establish
composting operations or other useful operations
Cloth waste: Annual production of cotton or rough
textile fibers wastes of one cotton mill ranges from
10 to 200 tons. Usually the waste is stored in the
municipal refuse depots in form of blended waste.
Increasing of the cotton yarn production results in
high amount of waste originated during cotton
processing and therefore there are searched ways
how that waste could be used
II. Experimental Procedure:
Teak leaves, sugarcane waste, cloth waste
are collected .All the wastes are firstly cleaned out
thoroughly with water to remove dirt and are dried
on open top for 15 days. The dried samples were cut
into small pieces (about ½ inch). The samples were
soaked in 3 different buckets for 24 hours. After 24
hrs the samples were filtered using a mesh and
partially dried for 15 min. The binder taken is Maida
(wheat flour). The amount of binder should be
added is known while making trails. We found
about 100 grams of Maida prepared will be
sufficient .In the hot water Maida flour is added
slowly and stirred vigorously Such that no lumps are
formed. Binder will attain the sticky nature. Maida
gives good strength to the samples and thus prevents
them from collapsing during firing. The water
filtered sample is mixed with the binder. Both are
mixed well. Then the mixture is kept into mould
which is placed on a wooden plank. After putting all
the prepared mixture the mould is closed with lid
and kept under fitted bench vise and tightened to
apply pressure. The pressure is applied for about 24
hours.After 24 hrs the mould should be carefully
removed. A rectangular briquette with high moisture
content is obtained. Then it should be dried enough
to obtain a rigid briquette. . During drying, the
Maida which would have formed a layer over the
particles, changes from a semi-solid to a solid form,
thus holding the particles together.
RESEARCH ARTICLE OPEN ACCESS
M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559
www.ijera.com 554 | P a g e
III. RESULTS AND DISCUSSIONS:
Characterization of briquettes:
XRD analysis: With the aid of two-positioned
STOE proportional sensitive detector (PSD), the x-
ray diffraction (XRD) patterns were recorded using
a STOE automatic powder diffractometer [22]. With
the use of Rietveld technique [23] the produced
patterns were refined (using match software) and the
matching compounds were detected.[24] . The
acquired graphs containing matching components at
different intensities are given below along with
matching components.
XRD graph of teak leaves XRD graph of Sugarcane waste
XRD graph of cloth waste
Scanning Electron Microscope:
SEM images of teak leaves sample:
SEM images of suagarcane sample:
M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559
www.ijera.com 555 | P a g e
SEM Images of Cloth waste sample
The morphology structure of the waste
briquettes was determined by using scanning
electron microscope. The morphological structure of
the teak leaves showed uniform short fibrous and
coarser structure. Whereas sugarcane wastes images
showed large and small dens granulated structures
respectively. Further image indicated long uniform
fibrous lingo cellulosic structure. The morphology
structure of material waste studies helps to predict
their agglomeration properties in order to be
briquetted.
Proximate analysis:
MOISTURE CONTENT: The total
energy that is needed to bring a briquette up to its
pyrolytic temperature is dependent on its moisture
content which affects the internal temperature
within the briquette due to endothermic evaporation
[1]. According to [2], moisture content is one of the
main parameters that determine briquette quality. A
lower moisture content of briquettes implies a
higher calorific value. The problem of too high
moisture content of the raw material can
significantly increase production costs. Biomass
moisture most often occurs as a result of inadequate
protection against atmospheric conditions during
storage. Particularly affected by this problem is the
raw material stored in the form of stacks. The
problem of too high raw-material moisture can be
solved using the dryers in the production process.
However, this solution requires investment, and
increases expenditures on production.[3]
The moisture content of raw biomass was
determined by calculating the loss in weight of
material using hot air oven dying method at 105℃
to 110℃ for one hour and up to constant weight loss
(Dara S.S.)[4]
𝑀𝑜𝑖𝑠𝑡𝑢𝑟𝑒 𝑐𝑜𝑛𝑡𝑒𝑛𝑡 %𝑤𝑏 =
𝑤2−𝑤3
𝑤2−𝑤1
× 100,
Where, w1 = weight of crucible, g w2 = weight of
crucible + sample, g w3 = weight of crucible +
sample after heating.
The moisture content of the cloth waste
briquette was determined to be 16.83, Sugarcane
waste, teak leaves briquettes have 16.40 and 15.82
respectively. A lower moisture content of briquettes
implies a higher calorific value. This is good forth
storability and combustibility of the briquettes as
recommended by [6]. From this we can say that
cloth waste will take more time for heating and will
have lower calorific value. Also it will be consumed
more for a certain heating purpose than other
briquettes .The value obtained is also corroborated
by [2] who reported a moisture content of 5% for
durable briquettes [7]. The total energy that is
needed to bring a briquette up to its pyrolytic
temperature is dependent on its moisture content
which affects the internal temperature within the
briquette due to endothermic evaporation [1].
ASH CONTENT: The residual sample in the
crucible was heated without lid in a muffle furnace
at 700 ± 50℃ for one half hour. The crucible was
then taken out, cooled first in air, then in desiccators
and weighed. Heating, cooling and weighing was
repeated, till a constant weight obtained. The residue
was reported as ash on percentage basis [4].
Ash content (%wb) =
𝑤3−𝑤1
𝑤2−𝑤1
×
100
Where, w1 = weight of the empty crucible, g w2 =
weight of empty crucible + sample, g w3 = weight
of the crucible + ash, g
Ash, which is the non-combustible
component of biomass, was found for waste cloth,
take leaves and sugarcane waste as 8.9, 19.4, 15
respectively. According to [11], ash has a significant
influence on the heat transfer to the surface of a fuel
M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559
www.ijera.com 556 | P a g e
as well as the diffusion of oxygen to the fuel surface
during char combustion. As ash is an impurity that
will not burn, fuels with low ash content are better
suited for thermal utilization than fuels with high
ash content. Higher ash content in a fuel usually
leads to higher dust emissions and affects the
combustion volume and efficiency. According to
[12], the higher the fuel's ash content, the lower is
its calorific value.[5]. Higher ash content in a fuel
usually leads to higher dust emissions and affects
the combustion volume and efficiency. According to
[4], the higher the fuel's ash content, the lower is its
calorific value. From the results we can say that
Teak leaves will have low calorific value.
VOLATILE MATTER:
Determination of volatile matter: The
dried sample left in the crucible was covered with a
lid and placed in an electric furnace (muffle
furnace), maintained at 925 ± 20℃ for 7 minutes.
The crucible was cooled first in air, then inside a
desiccators and weighed again. Loss in weight was
reported as volatile matter on percentage basis.
(Dara S.S.)
VOLATILEMATTER %WB =
W2−W3
W2−W1
× 100,
Where, w1 = weight of the empty crucible, g w2 =
weight of empty crucible + sample, g w3 = weight
of the crucible + sample after heating.
Biomass generally contains a high volatile
matter content of around 70% to 86% and low char
content. This makes biomass a highly reactive fuel
giving a faster combustion rate during the
devolatisation phase than other fuels such as coal
[15]. As reported by [16], low-grade fuels, such as
dung, tend to have low volatile content that results
in smoldering which other authors [17] described as
an incomplete combustion which leads to a
significant amount of smoke and release of toxic
gases. However, for the sawdust charcoal briquette,
a volatile content of 71% is high and an indication
of easy ignition of the briquette and proportionate
increase in flame length as suggested by [15]. The
high volatile matter content indicates that during
combustion, most of the teak leaves briquette will
volatize and burn as gas in the cook stove. From the
results Teak leaves have highly 57.78. So it will be
highly reactive fuel than the other two briquettes
which have lower volatile matter than it.
FIXED CARBON:The fixed carbon content of the
coal is the carbon found in the material that is left
after volatile materials are driven off. This differs
from the ultimate carbon content of the coal because
some carbon is lost in hydrocarbons with the
volatiles. Fixed carbon is used as an estimate of the
amount of coke that will be yielded from a sample
of coal. Fixed carbon is determined by removing the
mass of volatiles determined by the volatility test,
above, from the original mass of the coal sample. It
is used as %C in computation for calorific value.
Percentage of fixed carbon = 100 - % (moisture con-
tent+ volatile matter + ash)[4][10]
The fixed carbon of charcoal ranges from a
low of approximately 50% to a high of around 95%.
The charcoal for domestic use is recommended that
it should contain 80.5% of fixed carbon, while the
industrial charcoal is recommended to have 86.7%
of fixed carbon. On the other hand, the quality
smokeless domestic wood charcoal has been
specified to consist 75% of fixed carbon or more
than this while the industrial wood charcoal has
been specified to contain not less than 85% of fixed
carbon. The proportion of fixed carbon can be
controlled through maximum temperature and its
residence time during the carbonization process and
the charcoal produced from high temperature will be
higher in fixed carbon than the charcoal produced at
lower temperature. In addition, the charcoal having
high volatile matter has lower fixed carbon, which
low fixed carbon tends to be harder, heavier,
stronger and easier to ignite than charcoal
containing high fixed carbon [10].The briquettes
made from teak leaves, sugarcane waste and cloth
waste have 17.3, 18.9, 19.1.
M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559
www.ijera.com 557 | P a g e
ULTIMATE ANALYSIS:
The ultimate analysis indicates the various elemental chemical constituents such as carbon, hydrogen,
oxygen, sulphur, etc. It is useful in determining the quantity of air required for combustion and the volume and
composition of the combustion gases. The chemical compositions of composite waste briquettes include carbon,
hydrogen, oxygen, nitrogen and sulphur among others. The ultimate analysis or the determination of their
percentage compositions were carried out using standard methods. Thus, ASTM D5373-02 method was used for
the determination of percentage composition of carbon, hydrogen and nitrogen, ASTM D4239-02 method was
used for the determination of percentage composition of sulphur and ASTM D5142-02 method was used for the
determination of percentage ash content of individual composite briquette samples. The percentage oxygen
content of the individual composite agricultural waste briquette was determined by difference as follows . (1)
Where C, H,S, N ,O and Ash are the carbon, hydrogen, sulphur , nitrogen, oxygen and ash content of the
composite agricultural waste briquettes respectively [11]
%O=100-%(C+H+S+N+ASH)
The composition of the cloth waste briquette analyzed as showed 49.25% carbon, 4.698% hydrogen,
45.86% oxygen, 0.966% nitrogen and 0.154% sulphur. The results agree with the observations made by Chaney
[12] who reported that analysis of biomass using the gas analysis procedures revealed the principal constituent
as carbon, which comprises between 30% and 60% of the dry matter and typically 30% to 40% oxygen.
Hydrogen, being the third main constituent, makes up between about 5% and 6%, and nitrogen and sulphur (and
chlorine) normally make up less than 1% of dry biomass.
Other results of ultimate analysis for teak
leaves gave 48.879%, 4.826%, 35.139%,0.944%,
0.1096% for contents of carbon, hydrogen, oxygen,
nitrogen, and sulfur, respectively, while the
corresponding values for sugarcane waste briquette
in the order listed above were 44.926%, 4.1930%,
35.01%, 1.196%, and 0.295%, respectively.[13]
On average, the carbon and hydrogen
elements contents in the samples were found to be
47% and 4.57% respectively. These values are
higher than values of common low grade coal
reported by Guoqing Lu [14]. In general, the
increase in carbon and hydrogen content leads to an
increase in the HHV [15,16]. The mean percentage
of nitrogen available in the PS samples was
approximately 1%. The nitrogen content in PS was
found to be lower than coal as reported in [14], and
this decrease will fortunately doesn‟t require
Cloth waste
Teak Leaves
Sugarcane Waste
0
10
20
30
40
50
60
Cloth waste
Teak Leaves
Sugarcane Waste
0
50
100
150
%C %H %N %S %O
sugarcane waste
teak leaves
cloth waste
M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559
www.ijera.com 558 | P a g e
additional controls on temperature, pressure and air
concentration during the thermal conversion
process to reduce the NOX emissions. The mean
percentage of sulfur in the PS samples was almost
0.1, and this will results in low SO2 emissions from
incineration [14]. In general, the fuel
characterization results suggested that fuel
briquettes made from PS can be used in power
generation or process heating supply due to its high
calorific value and acceptable chemical
composition for emissions controls.[17]
The amount of carbon and hydrogen
content in the sample examined is an indication
that they will contribute immensely to the
combustibility of the briquette as suggested by
[18]. According to [19], the resulting composition
Of biomass affects its combustion characteristics as
the total overall mass of the fuel decreases during
the volatile combustion phase of the combustion
process, as the hydrogen to carbon ratio of the fuel
increases and, to a lesser extent, as the oxygen to
carbon ratio increases. Nitrogen, sulphur and
chlorine are significant in the formation of harmful
emissions and have an effect on reactions forming
ash [10]. The sulphur and nitrogen contents
reported which are below 1% is a welcome
development as there will be minimal release of
sulphur and nitrogen oxides into the atmosphere,
thereby limiting the polluting effect of the
briquettes [20][21].
Calorific Value: Heat value or calorific value
determines the energy content of a fuel. It is the
property of biomass fuel that depends on its
chemical composition and moisture content. The
most important fuel property is its calorific or heat
value [2]. The computed calorific value for the
cloth waste briquette was 6003 kJ/kg. Sugarcane
waste and cloth waste briquettes have 6239 and
6132 kJ/kg respectively. This energy value can
produce enough heat required for household
cooking and small-scale industrial cottage
applications.
Porosity Index: Porosity of the briquettes
increases with increase in the biomass
concentration. Biomass has higher inherent
porosity due to its fibrous nature coupled that after
pulverization, its particle sizes were relatively
bigger than that of coal. These two factors offered
it the ability of increasing the number of pores in
the briquette. The sample containing 0% biomass,
cloth waste has the least porosity index, 0.2211
while the one comprising 100% biomass, teak
leaves and sugarcane waste both have the high
porosity, 37.23 and 34.12. Low porosity will hinder
mass transfer during combustion due to fewer
spaces for mass diffusion. The higher the porosity,
the higher the rate of infiltration of oxidant and out
flow of combustion/pyrolysis products during
combustion and the higher will be the burning rate
of the briquette. [21]
Conclusion:
Good quality and highly storable/durable
briquettes can be produced from cloth waste, Teak
leaves and sugarcane waste.
1. Cloth waste briquette has high moisture content,
low in ash content and has high fixed carbon
amount than the other two briquettes. This
briquette may be unstable for longer periods
2. Teak leaves briquette has low moisture content
and high ash content. This briquette is ready to
burn due to high volatile matter and has high
calorific value
3. Sugarcane waste briquette is the stable briquette
which is stable for longer periods.
Therefore, it is recommended to use these
briquettes in small scale Industries and for
household purposes.
References:
[1.] Zaror, CA, Pyle, PD: The pyrolysis of
biomass: a general review. Sadhana Acad.
Proc. Eng. Sci. 5(4), 269–285 (1982)
[2.] Aina, OM, Adetogun, AC, Iyiola, KA: Heat
energy from value-added sawdust
briquettes of Albiziazygia. Ethiopian
Journal of Environmental Studies and
Management 2(1), 42–49 (2009)
[3.] Wojciech ŻARSKI “ economic aspects of
production of fuel briquette from agro
biomass” 2011, Issue 44, p134-143. 10p.
[4.] S. H. Sengar, A. G. Mohod1, Y. P.
Khandetod1, S. S. Patil2, A. D. Chendake “
Performance of Briquetting Machine for
Briquette Fuel” International Journal of
Energy Engineering 2012, 2(1): 28-34 DOI:
10.5923/j.ijee.20120201.05
[5.] Kim, HJ, Lu, GQ, Naruse, I, Yuan, J,
Ohtake, K: Modeling combustion
characteristics of bio-coal briquettes. J.
Energy Resour. Technol. 123, 27–31
(2001)
[6.] Loo, SV, Koppejan, J: The Handbook of
Biomass Combustion and Co-firing.
Earthscan, London (2008).
[7.] Joel Chaney “combustion characteristics of
briquettes” EWB-UK National Research &
Education Conference 2011 UK National
Research & Education Conference 2011
„Our Global Future‟ 4th March 2011
[8.] Hand book of loo and koppajen “biomass
combustion and co-firing” Issn-978-1-
84407-249-1.
M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com
ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559
www.ijera.com 559 | P a g e
[9.] Loo, SV, Koppejan, J: The Handbook of
Biomass Combustion and Co-firing. Earth
scan, London (2008)
[10.] Pallavi.H.V, Srikantaswamy.S*, Kiran
B.M, Vyshnavi.D.R and Ashwin.C.A
“Briquetting Agricultural Waste as an
Energy Source” JECET; December 12-
February 2013; Vol.2.No.1, 160-172.
[11.] Nicholas Akhaze Musa, “ Determination of
Chemical Compositions, Heating Value
and Theoretical Parameters of Composite
Agricultural Waste Briquettes”
International Journal of Scientific &
Engineering Research Volume 3, Issue 6,
June-2012 1 ISSN 2229-5518.
[12.] Chaney, J: Combustion Characteristics of
Biomass Briquettes. University of
Nottingham, Dissertation (2010)
[13.] J.T. Oladeji “Fuel Characterization of
Briquettes Produced from Corncob and
Rice Husk Resides.” The Pacific Journal of
Science and Technology Volume 11.
Number 1. May 2010 (Spring)
[14.] A. B. A. Ibrahima, M. S. Arisb, Y. S. Chin
“Development of Fuel Briquettes from
Dewatered Poultry Sludge” 2012
International Conference on Future
Electrical Power and Energy Systems
Lecture Notes in Information Technology,
Vol.9
[15.] C. Y. Yin, “Prediction of higher heating
values of biomass from proximate and
ultimate analyses,”Fuel 90, 1128-1132,
January 2010.
[16.] C. Sheng, J. L. T. Azvedeo,”Estimating the
higher heating value of biomass fuel from
basic analysis data, “Biomass and
bioenergy 28, 499-507, November 2004.
[17.] G. Lu, H. Kim, J. Yuan, I. Naruse, and K.
Ohtake, ”Experimental study on self –
Desulfurization characteristics of bio
briquettes in combustion, “Energy and
Fuels 12,689-696, 1998.
[18.] Musa, NA: Comparative fuel
characterization of rice husk and groundnut
shell briquettes. NJREDI 6(4), 23–27
(2007)
[19.] Grover, PD, Mishra, SK, Clancy, JS:
Development of an appropriate biomass
briquetting technology suitable for
production and use in developing countries.
Energy Sustain. Dev. 1(1), 45–48 (1994)
[20.] Enweremadu, CC, Ojediran, JO, Oladeji,
JT, Afolabi, LO: Evaluation of energy
potential in husks from soy-bean and
cowpea. Sci. Focus 8, 18–23 (2004)
[21.] Joseph O Akowuah1*, Francis
Kemausuor1 and Stephen J Mitchual2
“Physico-chemical characteristics and
market potential of sawdust charcoal
briquette” Akowuah et al. International
Journal of Energy and Environmental
Engineering 2012, 3:20
[22.] Wölfel, E. R., 1983, J. Appl. Crystallogr.,
16, pp 341-348.
[23.] Rietveld, H. M., 1969, J. Appl. Crytst. V2,
pp 65 – 71.
[24.] S. A. Ibitoye and A. A. Afonja
“Characterization of Cold Briquetted Iron
(CBI) By X-Ray Diffraction Technique”
Journal of Minerals & Materials
Characterization & Engineering, Vol. 7,
No.1, pp 39-48, 2007.

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Ct4301553559

  • 1. M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559 www.ijera.com 553 | P a g e Studies On Development Of Fuel Briquettes Using Locally Avaliable Waste Ch. A. I. Raju, M. Satya, U. Praveena and K. Ramya Jyothi Department of Chemical Engineering Andhra University, Visakhapatnam – 530 003 ABSTRACT: The Energy requirement is increasing day by day as the number of industries is increasing proportionately and the present power supply is unable to meet the energy demand. To combat this energy shortage, developed as well as developing countries are putting more efforts into R&D to tap alternative energy sources. State policies are also being formulated to encourage alternative sources of energy. In India alone, it is proposed that 17,000 MW should be produced from biomass. Although other options like gasification can be used for power generation, briquetting of biomass can be considered for its economics, reliability and ease of operation. Briquettes of small size can be used in gasifies for power generation. If the plant sites are chosen properly for easy availability of raw material, the agro-residues can be briquetted to reduce further transportation costs and associated pollution. This also improves the handling characteristics of biomass. The briquettes so obtained are very good fuels for local small scale industries and domestic purposes. Key Words: Fuel Briquettes, Proximate Analysis, Ultimate Analysis, XRD, SEM I. Material and methods: Sugarcane waste: India, as we all know is the second biggest sugarcane growing country in the World, only behind Brazil. Every year, 4 million hectares had been planted with sugarcane. Sugar plant can process 40 million tons sugarcane every year. For each tone of sugarcane crushed, about 300 kg of bagasse is retrieved. Previously bagasse is used as the fuel of sugar production. However only a third of bagasse are flamed, the remaining is discarded. That is to say, making bagasse into briquettes contains huge potential Teak leaves: The primary benefit of leaf and yard waste is the potential for immediate diversion of a significant portion of the state's solid waste stream from disposal facilities. The economic and environmental benefits which result from eliminating this material from disposal facilities and converting it to briquettes have provided municipalities with the incentive to establish composting operations or other useful operations Cloth waste: Annual production of cotton or rough textile fibers wastes of one cotton mill ranges from 10 to 200 tons. Usually the waste is stored in the municipal refuse depots in form of blended waste. Increasing of the cotton yarn production results in high amount of waste originated during cotton processing and therefore there are searched ways how that waste could be used II. Experimental Procedure: Teak leaves, sugarcane waste, cloth waste are collected .All the wastes are firstly cleaned out thoroughly with water to remove dirt and are dried on open top for 15 days. The dried samples were cut into small pieces (about ½ inch). The samples were soaked in 3 different buckets for 24 hours. After 24 hrs the samples were filtered using a mesh and partially dried for 15 min. The binder taken is Maida (wheat flour). The amount of binder should be added is known while making trails. We found about 100 grams of Maida prepared will be sufficient .In the hot water Maida flour is added slowly and stirred vigorously Such that no lumps are formed. Binder will attain the sticky nature. Maida gives good strength to the samples and thus prevents them from collapsing during firing. The water filtered sample is mixed with the binder. Both are mixed well. Then the mixture is kept into mould which is placed on a wooden plank. After putting all the prepared mixture the mould is closed with lid and kept under fitted bench vise and tightened to apply pressure. The pressure is applied for about 24 hours.After 24 hrs the mould should be carefully removed. A rectangular briquette with high moisture content is obtained. Then it should be dried enough to obtain a rigid briquette. . During drying, the Maida which would have formed a layer over the particles, changes from a semi-solid to a solid form, thus holding the particles together. RESEARCH ARTICLE OPEN ACCESS
  • 2. M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559 www.ijera.com 554 | P a g e III. RESULTS AND DISCUSSIONS: Characterization of briquettes: XRD analysis: With the aid of two-positioned STOE proportional sensitive detector (PSD), the x- ray diffraction (XRD) patterns were recorded using a STOE automatic powder diffractometer [22]. With the use of Rietveld technique [23] the produced patterns were refined (using match software) and the matching compounds were detected.[24] . The acquired graphs containing matching components at different intensities are given below along with matching components. XRD graph of teak leaves XRD graph of Sugarcane waste XRD graph of cloth waste Scanning Electron Microscope: SEM images of teak leaves sample: SEM images of suagarcane sample:
  • 3. M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559 www.ijera.com 555 | P a g e SEM Images of Cloth waste sample The morphology structure of the waste briquettes was determined by using scanning electron microscope. The morphological structure of the teak leaves showed uniform short fibrous and coarser structure. Whereas sugarcane wastes images showed large and small dens granulated structures respectively. Further image indicated long uniform fibrous lingo cellulosic structure. The morphology structure of material waste studies helps to predict their agglomeration properties in order to be briquetted. Proximate analysis: MOISTURE CONTENT: The total energy that is needed to bring a briquette up to its pyrolytic temperature is dependent on its moisture content which affects the internal temperature within the briquette due to endothermic evaporation [1]. According to [2], moisture content is one of the main parameters that determine briquette quality. A lower moisture content of briquettes implies a higher calorific value. The problem of too high moisture content of the raw material can significantly increase production costs. Biomass moisture most often occurs as a result of inadequate protection against atmospheric conditions during storage. Particularly affected by this problem is the raw material stored in the form of stacks. The problem of too high raw-material moisture can be solved using the dryers in the production process. However, this solution requires investment, and increases expenditures on production.[3] The moisture content of raw biomass was determined by calculating the loss in weight of material using hot air oven dying method at 105℃ to 110℃ for one hour and up to constant weight loss (Dara S.S.)[4] 𝑀𝑜𝑖𝑠𝑡𝑢𝑟𝑒 𝑐𝑜𝑛𝑡𝑒𝑛𝑡 %𝑤𝑏 = 𝑤2−𝑤3 𝑤2−𝑤1 × 100, Where, w1 = weight of crucible, g w2 = weight of crucible + sample, g w3 = weight of crucible + sample after heating. The moisture content of the cloth waste briquette was determined to be 16.83, Sugarcane waste, teak leaves briquettes have 16.40 and 15.82 respectively. A lower moisture content of briquettes implies a higher calorific value. This is good forth storability and combustibility of the briquettes as recommended by [6]. From this we can say that cloth waste will take more time for heating and will have lower calorific value. Also it will be consumed more for a certain heating purpose than other briquettes .The value obtained is also corroborated by [2] who reported a moisture content of 5% for durable briquettes [7]. The total energy that is needed to bring a briquette up to its pyrolytic temperature is dependent on its moisture content which affects the internal temperature within the briquette due to endothermic evaporation [1]. ASH CONTENT: The residual sample in the crucible was heated without lid in a muffle furnace at 700 ± 50℃ for one half hour. The crucible was then taken out, cooled first in air, then in desiccators and weighed. Heating, cooling and weighing was repeated, till a constant weight obtained. The residue was reported as ash on percentage basis [4]. Ash content (%wb) = 𝑤3−𝑤1 𝑤2−𝑤1 × 100 Where, w1 = weight of the empty crucible, g w2 = weight of empty crucible + sample, g w3 = weight of the crucible + ash, g Ash, which is the non-combustible component of biomass, was found for waste cloth, take leaves and sugarcane waste as 8.9, 19.4, 15 respectively. According to [11], ash has a significant influence on the heat transfer to the surface of a fuel
  • 4. M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559 www.ijera.com 556 | P a g e as well as the diffusion of oxygen to the fuel surface during char combustion. As ash is an impurity that will not burn, fuels with low ash content are better suited for thermal utilization than fuels with high ash content. Higher ash content in a fuel usually leads to higher dust emissions and affects the combustion volume and efficiency. According to [12], the higher the fuel's ash content, the lower is its calorific value.[5]. Higher ash content in a fuel usually leads to higher dust emissions and affects the combustion volume and efficiency. According to [4], the higher the fuel's ash content, the lower is its calorific value. From the results we can say that Teak leaves will have low calorific value. VOLATILE MATTER: Determination of volatile matter: The dried sample left in the crucible was covered with a lid and placed in an electric furnace (muffle furnace), maintained at 925 ± 20℃ for 7 minutes. The crucible was cooled first in air, then inside a desiccators and weighed again. Loss in weight was reported as volatile matter on percentage basis. (Dara S.S.) VOLATILEMATTER %WB = W2−W3 W2−W1 × 100, Where, w1 = weight of the empty crucible, g w2 = weight of empty crucible + sample, g w3 = weight of the crucible + sample after heating. Biomass generally contains a high volatile matter content of around 70% to 86% and low char content. This makes biomass a highly reactive fuel giving a faster combustion rate during the devolatisation phase than other fuels such as coal [15]. As reported by [16], low-grade fuels, such as dung, tend to have low volatile content that results in smoldering which other authors [17] described as an incomplete combustion which leads to a significant amount of smoke and release of toxic gases. However, for the sawdust charcoal briquette, a volatile content of 71% is high and an indication of easy ignition of the briquette and proportionate increase in flame length as suggested by [15]. The high volatile matter content indicates that during combustion, most of the teak leaves briquette will volatize and burn as gas in the cook stove. From the results Teak leaves have highly 57.78. So it will be highly reactive fuel than the other two briquettes which have lower volatile matter than it. FIXED CARBON:The fixed carbon content of the coal is the carbon found in the material that is left after volatile materials are driven off. This differs from the ultimate carbon content of the coal because some carbon is lost in hydrocarbons with the volatiles. Fixed carbon is used as an estimate of the amount of coke that will be yielded from a sample of coal. Fixed carbon is determined by removing the mass of volatiles determined by the volatility test, above, from the original mass of the coal sample. It is used as %C in computation for calorific value. Percentage of fixed carbon = 100 - % (moisture con- tent+ volatile matter + ash)[4][10] The fixed carbon of charcoal ranges from a low of approximately 50% to a high of around 95%. The charcoal for domestic use is recommended that it should contain 80.5% of fixed carbon, while the industrial charcoal is recommended to have 86.7% of fixed carbon. On the other hand, the quality smokeless domestic wood charcoal has been specified to consist 75% of fixed carbon or more than this while the industrial wood charcoal has been specified to contain not less than 85% of fixed carbon. The proportion of fixed carbon can be controlled through maximum temperature and its residence time during the carbonization process and the charcoal produced from high temperature will be higher in fixed carbon than the charcoal produced at lower temperature. In addition, the charcoal having high volatile matter has lower fixed carbon, which low fixed carbon tends to be harder, heavier, stronger and easier to ignite than charcoal containing high fixed carbon [10].The briquettes made from teak leaves, sugarcane waste and cloth waste have 17.3, 18.9, 19.1.
  • 5. M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559 www.ijera.com 557 | P a g e ULTIMATE ANALYSIS: The ultimate analysis indicates the various elemental chemical constituents such as carbon, hydrogen, oxygen, sulphur, etc. It is useful in determining the quantity of air required for combustion and the volume and composition of the combustion gases. The chemical compositions of composite waste briquettes include carbon, hydrogen, oxygen, nitrogen and sulphur among others. The ultimate analysis or the determination of their percentage compositions were carried out using standard methods. Thus, ASTM D5373-02 method was used for the determination of percentage composition of carbon, hydrogen and nitrogen, ASTM D4239-02 method was used for the determination of percentage composition of sulphur and ASTM D5142-02 method was used for the determination of percentage ash content of individual composite briquette samples. The percentage oxygen content of the individual composite agricultural waste briquette was determined by difference as follows . (1) Where C, H,S, N ,O and Ash are the carbon, hydrogen, sulphur , nitrogen, oxygen and ash content of the composite agricultural waste briquettes respectively [11] %O=100-%(C+H+S+N+ASH) The composition of the cloth waste briquette analyzed as showed 49.25% carbon, 4.698% hydrogen, 45.86% oxygen, 0.966% nitrogen and 0.154% sulphur. The results agree with the observations made by Chaney [12] who reported that analysis of biomass using the gas analysis procedures revealed the principal constituent as carbon, which comprises between 30% and 60% of the dry matter and typically 30% to 40% oxygen. Hydrogen, being the third main constituent, makes up between about 5% and 6%, and nitrogen and sulphur (and chlorine) normally make up less than 1% of dry biomass. Other results of ultimate analysis for teak leaves gave 48.879%, 4.826%, 35.139%,0.944%, 0.1096% for contents of carbon, hydrogen, oxygen, nitrogen, and sulfur, respectively, while the corresponding values for sugarcane waste briquette in the order listed above were 44.926%, 4.1930%, 35.01%, 1.196%, and 0.295%, respectively.[13] On average, the carbon and hydrogen elements contents in the samples were found to be 47% and 4.57% respectively. These values are higher than values of common low grade coal reported by Guoqing Lu [14]. In general, the increase in carbon and hydrogen content leads to an increase in the HHV [15,16]. The mean percentage of nitrogen available in the PS samples was approximately 1%. The nitrogen content in PS was found to be lower than coal as reported in [14], and this decrease will fortunately doesn‟t require Cloth waste Teak Leaves Sugarcane Waste 0 10 20 30 40 50 60 Cloth waste Teak Leaves Sugarcane Waste 0 50 100 150 %C %H %N %S %O sugarcane waste teak leaves cloth waste
  • 6. M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559 www.ijera.com 558 | P a g e additional controls on temperature, pressure and air concentration during the thermal conversion process to reduce the NOX emissions. The mean percentage of sulfur in the PS samples was almost 0.1, and this will results in low SO2 emissions from incineration [14]. In general, the fuel characterization results suggested that fuel briquettes made from PS can be used in power generation or process heating supply due to its high calorific value and acceptable chemical composition for emissions controls.[17] The amount of carbon and hydrogen content in the sample examined is an indication that they will contribute immensely to the combustibility of the briquette as suggested by [18]. According to [19], the resulting composition Of biomass affects its combustion characteristics as the total overall mass of the fuel decreases during the volatile combustion phase of the combustion process, as the hydrogen to carbon ratio of the fuel increases and, to a lesser extent, as the oxygen to carbon ratio increases. Nitrogen, sulphur and chlorine are significant in the formation of harmful emissions and have an effect on reactions forming ash [10]. The sulphur and nitrogen contents reported which are below 1% is a welcome development as there will be minimal release of sulphur and nitrogen oxides into the atmosphere, thereby limiting the polluting effect of the briquettes [20][21]. Calorific Value: Heat value or calorific value determines the energy content of a fuel. It is the property of biomass fuel that depends on its chemical composition and moisture content. The most important fuel property is its calorific or heat value [2]. The computed calorific value for the cloth waste briquette was 6003 kJ/kg. Sugarcane waste and cloth waste briquettes have 6239 and 6132 kJ/kg respectively. This energy value can produce enough heat required for household cooking and small-scale industrial cottage applications. Porosity Index: Porosity of the briquettes increases with increase in the biomass concentration. Biomass has higher inherent porosity due to its fibrous nature coupled that after pulverization, its particle sizes were relatively bigger than that of coal. These two factors offered it the ability of increasing the number of pores in the briquette. The sample containing 0% biomass, cloth waste has the least porosity index, 0.2211 while the one comprising 100% biomass, teak leaves and sugarcane waste both have the high porosity, 37.23 and 34.12. Low porosity will hinder mass transfer during combustion due to fewer spaces for mass diffusion. The higher the porosity, the higher the rate of infiltration of oxidant and out flow of combustion/pyrolysis products during combustion and the higher will be the burning rate of the briquette. [21] Conclusion: Good quality and highly storable/durable briquettes can be produced from cloth waste, Teak leaves and sugarcane waste. 1. Cloth waste briquette has high moisture content, low in ash content and has high fixed carbon amount than the other two briquettes. This briquette may be unstable for longer periods 2. Teak leaves briquette has low moisture content and high ash content. This briquette is ready to burn due to high volatile matter and has high calorific value 3. Sugarcane waste briquette is the stable briquette which is stable for longer periods. Therefore, it is recommended to use these briquettes in small scale Industries and for household purposes. References: [1.] Zaror, CA, Pyle, PD: The pyrolysis of biomass: a general review. Sadhana Acad. Proc. Eng. Sci. 5(4), 269–285 (1982) [2.] Aina, OM, Adetogun, AC, Iyiola, KA: Heat energy from value-added sawdust briquettes of Albiziazygia. Ethiopian Journal of Environmental Studies and Management 2(1), 42–49 (2009) [3.] Wojciech ŻARSKI “ economic aspects of production of fuel briquette from agro biomass” 2011, Issue 44, p134-143. 10p. [4.] S. H. Sengar, A. G. Mohod1, Y. P. Khandetod1, S. S. Patil2, A. D. Chendake “ Performance of Briquetting Machine for Briquette Fuel” International Journal of Energy Engineering 2012, 2(1): 28-34 DOI: 10.5923/j.ijee.20120201.05 [5.] Kim, HJ, Lu, GQ, Naruse, I, Yuan, J, Ohtake, K: Modeling combustion characteristics of bio-coal briquettes. J. Energy Resour. Technol. 123, 27–31 (2001) [6.] Loo, SV, Koppejan, J: The Handbook of Biomass Combustion and Co-firing. Earthscan, London (2008). [7.] Joel Chaney “combustion characteristics of briquettes” EWB-UK National Research & Education Conference 2011 UK National Research & Education Conference 2011 „Our Global Future‟ 4th March 2011 [8.] Hand book of loo and koppajen “biomass combustion and co-firing” Issn-978-1- 84407-249-1.
  • 7. M. Satya et al Int. Journal of Engineering Research and Applications www.ijera.com ISSN : 2248-9622, Vol. 4, Issue 3( Version 1), March 2014, pp.553-559 www.ijera.com 559 | P a g e [9.] Loo, SV, Koppejan, J: The Handbook of Biomass Combustion and Co-firing. Earth scan, London (2008) [10.] Pallavi.H.V, Srikantaswamy.S*, Kiran B.M, Vyshnavi.D.R and Ashwin.C.A “Briquetting Agricultural Waste as an Energy Source” JECET; December 12- February 2013; Vol.2.No.1, 160-172. [11.] Nicholas Akhaze Musa, “ Determination of Chemical Compositions, Heating Value and Theoretical Parameters of Composite Agricultural Waste Briquettes” International Journal of Scientific & Engineering Research Volume 3, Issue 6, June-2012 1 ISSN 2229-5518. [12.] Chaney, J: Combustion Characteristics of Biomass Briquettes. University of Nottingham, Dissertation (2010) [13.] J.T. Oladeji “Fuel Characterization of Briquettes Produced from Corncob and Rice Husk Resides.” The Pacific Journal of Science and Technology Volume 11. Number 1. May 2010 (Spring) [14.] A. B. A. Ibrahima, M. S. Arisb, Y. S. Chin “Development of Fuel Briquettes from Dewatered Poultry Sludge” 2012 International Conference on Future Electrical Power and Energy Systems Lecture Notes in Information Technology, Vol.9 [15.] C. Y. Yin, “Prediction of higher heating values of biomass from proximate and ultimate analyses,”Fuel 90, 1128-1132, January 2010. [16.] C. Sheng, J. L. T. Azvedeo,”Estimating the higher heating value of biomass fuel from basic analysis data, “Biomass and bioenergy 28, 499-507, November 2004. [17.] G. Lu, H. Kim, J. Yuan, I. Naruse, and K. Ohtake, ”Experimental study on self – Desulfurization characteristics of bio briquettes in combustion, “Energy and Fuels 12,689-696, 1998. [18.] Musa, NA: Comparative fuel characterization of rice husk and groundnut shell briquettes. NJREDI 6(4), 23–27 (2007) [19.] Grover, PD, Mishra, SK, Clancy, JS: Development of an appropriate biomass briquetting technology suitable for production and use in developing countries. Energy Sustain. Dev. 1(1), 45–48 (1994) [20.] Enweremadu, CC, Ojediran, JO, Oladeji, JT, Afolabi, LO: Evaluation of energy potential in husks from soy-bean and cowpea. Sci. Focus 8, 18–23 (2004) [21.] Joseph O Akowuah1*, Francis Kemausuor1 and Stephen J Mitchual2 “Physico-chemical characteristics and market potential of sawdust charcoal briquette” Akowuah et al. International Journal of Energy and Environmental Engineering 2012, 3:20 [22.] Wölfel, E. R., 1983, J. Appl. Crystallogr., 16, pp 341-348. [23.] Rietveld, H. M., 1969, J. Appl. Crytst. V2, pp 65 – 71. [24.] S. A. Ibitoye and A. A. Afonja “Characterization of Cold Briquetted Iron (CBI) By X-Ray Diffraction Technique” Journal of Minerals & Materials Characterization & Engineering, Vol. 7, No.1, pp 39-48, 2007.