5. Pyrolysis oil:-
ü Pyrolysis oil, sometimes also known as biocrude or bio-oil, is a synthetic
fuel under investigation as substitute for petroleum.
OR
ü Pyrolysis oil is the end product of waste plastic and tyre pyrolysis. Pyrolysis oil is
widely used as industrial fuel to substitute furnace oil or industrial diesel.
Tyre pyrolysis oil:-
ü The pyrolysis oil is extracted from waste tyre or waste plastic by our pyrolysis plant,
the pyrolysis plant is a machine converts waste tyre to oil
ü During the process of converting waste tyre/plastic to fuel oil there will be no
pollution and solid waste. The end product of pyrolysis plant is fuel oil, carbon
black, and oil gas.
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6. Preparation of tyre pyrolysis oil:-
ü Initially an automobile tyre was cut into a number
of pieces and the bead, steel wires and fabrics were
removed. Thick rubber at the periphery of the tyre
was alone made into small chips.
ü The tyre chips were washed, dried and fed in to a
mild steel pyrolysis reactor unit.
ü The pyrolysis reactor used was a full insulated
cylindrical chamber of inner diameter 110 mm and
outer diameter 115 mm and height 300 mm.
ü Vacuum was created in the pyrolysis reactor and
then externally heated by means of 1.5 kW heaters.
The process was carried out between 450°C and
650°C in the reactor for 2 hours and 30 minutes.
ü The products of pyrolysis in the form of vapour
were sent to a water cooled condenser and the
condensed liquid was collected as a fuel. The non
condensable gases were let out to atmosphere.
ü The TPO collected was crude in nature. For an
output of 1 kg of TPO about 2.09 kg of waste tyres
feedstock was required.
ü The heat energy required to convert the waste tyres
into the products was around 7.8 MJ/kg. The
residence time of the pyrolysis process was 90
minutes.
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7. Preparation of pyrolysis tyre oil:-
ü Initially an automobile tyre was cut into a number of pieces and the bead, steel wires
and fabrics were removed. Thick rubber at the periphery of the tyre was alone made
into small chips.
ü The tyre chips were washed, dried and fed in to a mild steel pyrolysis reactor unit.
ü The pyrolysis reactor used was a full insulated cylindrical chamber of inner diameter
110 mm and outer diameter 115 mm and height 300 mm.
ü Vacuum was created in the pyrolysis reactor and then externally heated by means of
1.5 kW heaters. The process was carried out between 450°C and 650°C in the
reactor for 2 hours and 30 minutes.
ü The products of pyrolysis in the form of vapour were sent to a water cooled
condenser and the condensed liquid was collected as a fuel. The non condensable
gases were let out to atmosphere.
ü The TPO collected was crude in nature. For an output of 1 kg of TPO about 2.09 kg
of waste tyres feedstock was required.
ü The heat energy required to convert the waste tyres into the products was around 7.8
MJ/kg. The residence time of the pyrolysis process was 90 minutes.
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8. Experimental Setup:- Engine Test Ring
ü The setup is provided with necessary instruments
like Rope brake dynamometer, Smoke meter Gas
analyzer ,etc., for performance and emission
analysis.
ü Experimental Procedure:-
A. Performance, exhaust emission and combustion
tests were carried out on the CI engine using
blends of TPO-DF. All tests were conducted by
starting the engine with DF only.
B. After the engine was warmed up, it was then
switched to TPO-DF blend.
C. At the end of the test, the fuel was switched
back to diesel and the engine was kept running
for some time to flush out the TPO-DF blend by
DF from the fuel line and the injection system,
in order to prevent the fuel system from the
accumulation of TPO-DF which may damage
the system.
KEYWORD:-
TPO-Tyre pyrolysis oil & DF-Diesel fuel
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FIG-Engine Set up
[Yonus et al. (2013)]
10. Results of above experiment:-
• Performance study:-
1. Brake thermal efficiency:-
ü The brake thermal efficiency with
brake power for TPO-DF blends is
compared with the DF and shown in
Figure below.
ü The brake thermal efficiency for DF
at full load is 29.46 % while with
TPO 10 and TPO 30 it is 28.68 %
and 28.93 % respectively.
ü The brake thermal efficiency for
TPO 50 is 28.39 %.
ü TPO 30 shows a better performance
at all loads compared to TPO 10 and
TPO 50. The reason may be
additional lubricity.
ü In general, the engine operated with
TPO-DF blends give brake thermal
efficiencies marginally higher than
DF.
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11. Brake thermal efficiency:-
ü The variation of brake thermal
efficiency with brake power is
shown in fig. 2.from the the plot
it is observed that as the the
load increases the brake thermal
efficiency increases.
ü At full load condition the brake
thermal efficiency obtained are
23%, 26.07%,24.88%, for fuels
of diesel,TP10,TP20,TP30
respectively.
ü The brake thermal efficiency of
tyre oil blend TP020 increased
when compared to the diesel at
full load condition.
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12. Brake specific fuel consumption:-
ü The plot it is reveals that as the
the load increases the fuel
consumption decreases.
ü At full load condition the BSFC
obtained are 0.36kg/kw-hr, 0.32
kg/kw-hr,0. 34kg/kw-hr
,0.32kg/kw-hr ,034kg/kw-
hr,0.2966kg/kw -hr and
0.32kg/kw-hr for fuels of
diesel,TP10,TP20,TP30 ,TPE
10,TPE 20 &TPE30
respectively.
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14. Emissions Study:-
ü NOx Emissions:-
ü The variation of NOx emission
with brake power is shown in
fig.the plot it is reveals that as
the the load increases the NOx
emission decreases.
ü At full load condition the NOx
emissions obtained are :
680ppm,782ppm,743ppm. .
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17. NOMENCLATURE:-
ü B.P Brake Power
ü BSFC Brake Specific Fuel Consumption
ü BTH Brake Thermal Efficiency
ü CO Carbon Monoxide
ü NOx Oxides Of Nitrogen
ü TP 10 TYRE PYROLYSIS OIL 10%,ETHANOL 5%,EHN
0.5%,DIESEL 84.5%
ü TP 20 TYRE PYROLYSIS OIL 20%,ETHANOL 5%,EHN
0.5%,DIESEL 74.5%
ü TP 30 TYRE PYROLYSIS OIL 30%,ETHANOL 5%,EHN
0.5%,DIESEL 64.5%
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