Experimental investigation on diesel engine using fish oil biodiesel and its diesel blends.
Karthikeyan, A. ; Prasad, B. Durga
Introduction
The world is on the brink of energy crisis. The limited fossil fuel
sources are unable to provide for the continuously increasing demand of
energy. This associated with increasing price of fossil fuels and the
awareness of the impacts of environmental pollution and global warming,
has forced a search for an alternative source of energy, which is
renewable, safe and non-polluting. (1, 2) Since compression ignition
(CI) engines are more widely used compared to spark ignition (SI)
engines, greater attention is being devoted to develop an alternative
source of fuel for the same. Since vegetable oils and animal fats
satisfy the major requirements, necessary for a diesel engine fuel,
their suitability as alternative to diesel fuel have been a topic of
research. However, their higher viscosity and storage ability issues
restrict their direct use as alternate fuels (1, 2)
The use of vegetable oils in I.C engines dates back to 1900 when
Rudolph diesel, the inventor of compression ignition engines, used
peanut oil as an engine fuel. The energy crises of 1974 brought pressure
on various nations to search for non petroleum based alternate fuels.
Since then many vegetable oils of commercial and non commercial have
been tried and possible difficulties identified. The observed major
differences between diesel fuel and vegetable oil, included, for the
latter, the significantly higher viscosities and moderately higher
densities, lower heating values, rise in the stoichiometric fuel/air
ratio due the presence of molecular oxygen and the possibility of
thermal cracking at the temperatures encountered by the fuel spray in
naturally aspirated diesel engines (2). These differences contribute to
the poor atomization, choking tendencies, carbon deposits, heavy smoke
emissions and wear that were generally experienced and which adversely
affect the durability of the engine (3, 4 and 5).
Most research on biodiesel has focused on using plant based oils as
feed stocks. There has been much less research on converting
animal-based oils into biodiesel (6). One potential source of oil is
fish oil. It has been estimated that over a million tons of fish
by-products are generated from the fishing industry. Some of these
products are converted into fish meal and oil, but approximately 60% are
not utilized. The major fish by-products include fish heads, viscera and
some frames, with much of oil stored in the head (5). Fish by-products
can also be converted into hydrolysate through hydrolysis. Hydrolysis
involves multiple enzyme and heat treatments to break down proteins into
smaller peptides. The final hydrolysate product is usually stabilized by
acidification and can be used as fertilizer or as feed ingredients.
Hydrolysates of fish by-products contain a significant amount of oil,
which can be extracted and converted into biodiesel. (7)
The objective of this work was to study the performance, emission
and combustion characteristics of a single cylinder, direct injection
diesel engine using fish oil biodiesel and their blends with diesel in
varying proportions. The results were compared with the results obtained
for diesel.
Materials and Methods
Production of the biodiesel from the refined fish oil
Several technologies are available to manufacture biodiesel, such
as transesterification, amidation with diethylamine, catalyzing
pyrolysis, and transesterification in supercritical methanol. Of these
techniques, transesterification is the most widely applied in industrial
biodiesel production. Three types of catalysts can be used in the
transesterification process: a strong alkali, strong acid or enzyme. A
strong alkali catalyst is frequently used in the transesterification
reaction due to its dominant advantages of a shorter reaction time and
smaller amount of catalyst required (8).
The refined fish oil was transesterified with methyl alcohol to
produce biodiesel. Sodium methoxide was prepared by mixing 25% (by
volume of oil) of pure methanol and 6.25g (Per liter of oil) of sodium
hydroxide (NaOH). The sodium methoxide, which played a role of enhancing
the transesterification process was poured in to a reaction vessel and
mixed with the refined fish oil. To prevent the methanol from being
vaporized by the reactant mixture, the reacting temperature was fixed at
60[degrees]C, which is just below the boiling point of methanol at
63[degrees]C. The mixing was done for 50 to 60 minutes. Then the mixture
was poured in to a separating funnel and it was allowed to rest for 12
hours. The glycerin was formed at the bottom and the bio-diesel at the
top. Bio-diesel was separated from the glycerin. Finally, it was washed
and dried to remove the excess alcohol.
Experimental setup
A vertical water cooled single cylinder four stroke, direct
injection diesel engine was used for this study. The engine was coupled
with eddy current dynamometer for load measurement. The smoke density
was measured using AVL smoke meter. N[O.sub.x] emissions were measured
using exhaust gas analyzer. Particulate matter was measured using high
volume sampler. Experiments were conducted with pure diesel, pure
biodiesel and the blends of biodiesel with diesel.
Results and discussions
Experiments were conducted when the engine was fuelled with fish
oil biodiesel and their blends with diesel in proportions of 20:80,
40:60, 60:40 and 100% (by volume), which are generally called as B-20,
B-40, B-60 and B-100 respectively. The experiment covered a range of
loads.
The performance of the engine was evaluated in terms of brake
specific fuel consumption, brake thermal efficiency, volumetric
efficiency and air fuel ratio. The combustion characteristics of the
engine were studied in terms of cylinder pressure and rate of pressure
rise with respect to crank angle. The emission characteristics of the
engine were studied in terms exhaust gas temperature, concentration of
NOx, CO, particulate matter and smoke density. The results obtained for
Fish oil biodiesel and their blends with diesel were compared with the
results of diesel.
Brake specific fuel consumption
The result for the variations in the brake specific fuel
consumption (BSFC) is presented in the fig.1. For all the fuels the BSFC
falls with increasing load. The differences of BSFC are very small when
using different fuels. The minimum BSFC values are 0.34 kg/kW hr for
diesel, 0.37 kg/kW hr for B-20, 0.38 kg/kW hr for B-60 and 0.4 kg/kW hr
for B-100. The higher BSFC values in the case of pure Fish oil biodiesel
are due to their low energy content.
[FIGURE 1 OMITTED]
Brake thermal efficiency
The variation of brake thermal efficiency with load is shown in
fig. 2. Brake thermal efficiency gives an idea of the output generated
by the engine with respect to heat supplied in the form of fuel. For all
the fuels the brake thermal efficiency increases with load. The brake
thermal efficiency values at full load are 25.52% for diesel, 23.37% for
B-20, 22.64% for B-40, 25.57 For B-60 and 23.82% for B-100. The brake
thermal efficiencies of B-60 and B-100 are very close to the brake
thermal efficiencies of diesel at all loads. This may be due to their
low heat input requirement for higher power output at a given load.
[FIGURE 2 OMITTED]
Volumetric efficiency
The fig.3 shows the variation of volumetric efficiency with load
for various blends. Volumetric efficiency is a measure of success with
which the air supply, and thus the charge, is inducted in to the engine.
It indicates the breathing capacity of the engine. From the figure it is
evident that the volumetric efficiency values of B-40, B-60 and B-100
are exceeding the volumetric efficiency values of diesel at all loads.
[FIGURE 3 OMITTED]
Air fuel ratio
Fig.4 shows the variation of air-fuel ratio with load. In C.I
engines at a given speed the air flow do not vary with load, it is the
fuel flow that varies directly with load. From the figure it can be seen
that, air fuel ratio values of fish oil biodiesel and its diesel blends
are slightly less than diesel.
[FIGURE 4 OMITTED]
Exhaust gas Temperature
Fig.5 shows the variation of exhaust gas temperature with load for
various test fuels. It is observed that the exhaust gas temperature
increases with load because more fuel is burnt at higher loads to meet
the power requirement. It is also observed that the exhaust temperature
increases for B-20 and B-40 blends at all loads. This may be due to the
oxygen content of the biodiesel, which improves combustion and thus may
increase the exhaust gas temperature. But the exhaust gas temperatures
of B-60 blend and B-100 are very close to the exhaust temperature of
diesel and even less than diesel at higher loads. This reduction in
exhaust gas temperature for B-60 and B-100 at higher loads may be due to
their high latent heat of vaporization than the diesel fuel.
[FIGURE 5 OMITTED]
N[O.sub.x] emission
Fig.6 shows gradual increase in emission of nitrogen oxides
(N[O.sub.x]) with increase in percentage of fish oil biodiesel in the
fuel. The N[O.sub.x] emission increase for biodiesel may be associated
with the oxygen content of the biodiesel, since the oxygen present in
the fuel may provide additional oxygen for N[O.sub.x] formation. Another
factor causing the increase of N[O.sub.x] could be the possibility of
higher combustion temperature arising from improved combustion. The
N[O.sub.x] emission is found to be lower for diesel.
[FIGURE 6 OMITTED]
Smoke density
Fig.7 shows the variation of smoke density with brake power for
various test fuels. A reduction is observed with increase in percentage
of fish oil biodiesel in the fuel. This may be due to improved
combustion characteristics of biodiesel. It is observed that smoke
density is lower for pure fish oil biodiesel.
[FIGURE 7 OMITTED]
CO Emission
Fig.8 shows the reduction of CO emission with the addition of fish
oil biodiesel to diesel. CO is predominantly formed due to the lack of
oxygen. Since biodiesel is an oxygenated fuel, it leads to better
combustion of fuel resulting in decrease in CO emission. The CO emission
is found to be lower for pure fish oil biodiesel.
[FIGURE 8 OMITTED]
Particulate matter
Particulate emissions are as a result of incomplete combustion.
Fig.9 shows the particulate matter emission decreases with increase in
percentage of biodiesel in the fuel. Since biodiesel is an oxygenated
fuel, it promotes better combustion and results in reduction of
particulate matter emissions. The particulate emission is lower for pure
fish oil biodiesel.
[FIGURE 9 OMITTED]
Pressure variation with Crank angle
The pressure variation in the cycle is important in the analysis of
the performance characteristics of any fuel. Fig.10 and 11 shows the
variation of cylinder pressure with crank angle for various fuels at
rated load. Similar trends are observed for other loads also. Fish oil
biodiesel and its diesel blends exhibit slightly lower pressure at all
crank angles compared to diesel. The peak pressure values are 69.5 bar
for diesel, 67.31 for B20, 68.16 bar for B40, 67.48 bar for B60 and
67.99 bar for B100. The peak pressures for diesel, B60 and B100 occur at
13[degrees] after TDC. The peak pressures for B20 and B40 occur at
11[degrees] after TDC.
[FIGURE 10 OMITTED]
[FIGURE 11 OMITTED]
Rate of Pressure Rise
Fig.12 shows rate of pressure rise with crank angle at rated load
for test fuels. All the tests are performed at an injection timing
23[degrees] before top dead centre (bTDC). It can be observed that the
rate of pressure rise for Fish oil biodiesel and its diesel blends are
higher compared to diesel. The maximum rate of pressure rise is for B60
and B100. This may be due to improved combustion characteristics of
biodiesel and its Diesel blends.
[FIGURE 12 OMITTED]
Conclusions
Following are the conclusions based on the experimental results
obtained while operating single cylinder diesel engine fuelled with
biodiesel from fish oil and its diesel blends.
* Fish oil biodiesel and its diesel blends can be directly used in
diesel engines without any modifications.
* Brake specific fuel consumption values of fish oil biodiesel and
its diesel blends are slightly higher than diesel.
* Brake thermal efficiency of B60 blend and B-100 are very close to
the brake thermal efficiency of diesel at all loads.
* Volumetric efficiency values of fish oil biodiesel and its diesel
blends are exceeding the volumetric efficiency values of diesel at all
loads.
* Smoke, CO and particulate matter emissions decrease with increase
in percentage of fish oil biodiesel in the fuel.
* N[O.sub.x] emissions of fish oil biodiesel and its diesel blends
are slightly higher than that of diesel.
* Fish oil biodiesel and its diesel blends exhibit slightly lower
pressure at all crank angles compared to diesel. The peak pressure value
of B40 blend is very close to diesel.
* Rate of pressure rise for fish oil biodiesel and its diesel
blends are higher compared to diesel. The maximum rate of pressure rise
is for B60 and B100.
* From the above analysis the main conclusion is fish oil biodiesel
and its diesel blends are suitable substitute for diesel as they produce
lesser emissions than diesel and have satisfactory combustion and
performance characteristics.
Engine details:
Kirloskar TV1 Engine
Engine specification:
Type of engine : Vertical, 4stroke
Water cooled
Rated power : 5.2 @1500rpm
Cylinder diameter : 0.0875 m
Stroke length : 0.11 m
Compression ratio : 17.5: 1
Injection timing : 23[degrees] bTDC
Air measurement
Orifice diameter : 0.02 m
Eddy current dynamometer
Dynamometer arm length : 0.195 m
Nomenclature
N[O.sub.x] = Oxides of Nitrogen HSU = Hatridge Smoke Unit BSFC =
Brake Specific Fuel Consumption TDC = Top Dead Centre B20 = 20%
Biodiesel+80% Diesel B40 = 40% Biodiesel+60% Diesel B60 = 60%
Biodiesel+40% Diesel B100 = 100% Diesel.
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A. Karthikeyan (a), * and B. Durga Prasad (b)
(a) Sathyabama University, Chennai, Tamil Nadu, India
(b) J.N.T.U College of Engineering, Anatapur, A.P, India
* E-mail address: karthikeyan_sist@yahoo.co.in
Table 1: Fuel properties.
Properties Diesel Fish oil biodiesel
Kinematic viscosity at 40[degrees]C (Cst) 3.52 4.96
Density at 15[degrees]C (kg/[m.sup.3]) 830 850
Flash point ([degrees]C) 49 162
Cetane number 50 51
Calorific value (kJ/kg) 43000 37800
Total sulphur (% by mass) 0.01 0.05
Distillation (% by volume) 90 at 333[degrees]C
Ash (% by mass) 0.01 Nil
Oil ester (biodiesel) % 89.96