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International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169
Volume: 6 Issue: 6 57- 62
______________________________________________________________________________________
57
IJRITCC | June 2018, Available @ http://www.ijritcc.org
______________________________________________________________________________________
Effect of Tyre Pyrolysis Oil (TPO) Blends on Performance of Single Cylinder
Diesel Engine
P M bhatt
Mechanical Department, Gujarat technological University
Government Polytechnic, Ahmedabad, Gujarat, India
pmbhatt009@gmail.com
Abstract— Increasing industrialization and motorization led to a significant rise in demand of petroleum products. As these are the non-
renewable resources, it will be troublesome to predict the availability of these resources in the future, resulting in uncertainty in its supply and
price and is impacting growing economies like India importing 80% of the total demand of the petroleum products. Many attempts have been
made by different researchers to find out alternate fuels for Internal Combustion engines. Many alternate fuels like Biodiesel, LPG (Liquefied
Petroleum Gas), CNG (Compressed Natural Gas) and Alcohol are being used nowadays by different vehicles. In this context pyrolysis of scrap
tyres can be used effectively to produce oil, thereby solving the problem of waste tyre disposal. In the present study, Experimental investigations
were carried out to evaluate the performance and emission characteristics of a single cylinder diesel engine fueled by TPO10, TPO15, and
TPO20 at a crank angle 260
before TDC (Top Dead Centre) and injection pressure of 200 bar keeping the blend quality by controlling the
density and viscosity of tyre pyrolysis oil within permissible limit of euro IV diesel requirement. The performance and emission results were
analyzed and compared with that of diesel fuel operation. The results of investigations indicate that the brake thermal efficiency of the TPO - DF
blend decreases by 6 to 10%. CO emissions are slightly higher but well within permissible limit of euro IV emission standards. HC emissions
are higher by about 25 to 35% at partial load whereas smoke opacity is lower by about 3% to 21% as compared to diesel fuel.
Keywords— Experimental Investigation, Diesel Engine, Tyre Pyrolysis Oil (TPO), Performance, Emission
__________________________________________________*****_________________________________________________
I. INTRODUCTION
Petroleum based fuels are stored fuels in the earth. There are
limited reserves of these stored fuels and they are
irreplaceable. This finite resource of petroleum are highly
concentrated in certain regions of the world, have given rise to
uncertainty in its supply and price and is impacting growing
economies like India, importing 80% of the total demand of
crude. India’s petroleum product consumption has increased
from 100.4 million tonnes in 2001-02 to 133.4 million tonnes
in 2008-09 at a CAGR of 4.1% and is likely to increase up to
217 million tonnes by 2020-21 and 325.6 million tonnes by
2030-31. All over the world, there are initiatives to replace
gasoline and diesel fuel due to the impact of the fossil fuel
crisis and hike in oil price. Millions of dollars are being
invested in the search for alternative fuels. On the other hand,
the disposal of waste tyres from automotive vehicles is
becoming more and more complex. Waste to energy is the
recent trend in the selection of alternate fuels. Fuels like
alcohol, biodiesel, liquid fuel from plastics, etc. are some of
the alternative fuels for the internal combustion engines. In
order to prevent waste rubber and in particular discarded
automobile tyres from damaging the environment, it is highly
desirable to recycle this material in a useful manner. However,
the total quantity of tyres currently recycled in a given year
(excluding reuse, retreading, or combustion) is less than 7% of
the annual tyre generation rate in the world. The use of tyre
pyrolysis oil as a substitution of diesel fuel is an opportunity in
minimizing the utilization of the natural resources. Several
research works have been carried out on the pyrolysis of waste
automobile tyres. Pyrolysis is the process of thermally
degrading a substance into smaller, less complex molecules.
Pyrolysis produces three principle products: such as pyrolytic
oil, gas and char. The quality and quantity of these products
depend upon the reactor temperature and design. In the
Pyrolysis process, larger hydrocarbon chains break down at
certain temperatures in the absence or a limited supply of
oxygen that gives end products usually containing solids,
liquids and gases. If the temperature is maintained at 550 ºC,
the main product is a liquid, which could be a mixture of
various hydrocarbons depending on the initial composition of
the waste material. At temperatures above 700 ºC, the gas
becomes the primary product due to further cracking of
liquids. The gas is basically composed of CH4, with C2H6,
C2H4, C2H2, and other gaseous hydrocarbons however in lesser
quantities. In the present work pyrolysis oil from waste tyres
by pyrolysis is obtained and used as a blended fuel in
stationary diesel engine. Though solid carbon black and
pyrolysis gas are also obtained, the pyrolysis process will be
much more prominent to produce liquid [1, 2, 3, 4, and 5].
II. PREPARATION AND TESTING OF TYRE OIL
A. Pyrolysis of Waste Automobile Tyres
International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169
Volume: 6 Issue: 6 57- 62
______________________________________________________________________________________
58
IJRITCC | June 2018, Available @ http://www.ijritcc.org
______________________________________________________________________________________
Fig. 1 Waste Tyre Recycling Pyrolysis Plant
Pyrolysis is a Thermo chemical decomposition of organic
material at elevated temperature in the absence of oxygen.
Pyrolysis typically occurs under pressure and at operating
temperatures about 4300
C in a batch process system. In the
present work waste automobile tyres were fed into 5Tonnes
capacity rotary horizontal direct heating reactor vessel as
shown in figure 1. Initially the heat was supplied by means of
oil under controlled conditions of temperature and pressure.
The process resulted in molecular restructuring of rubber and
converted into vapours and gases. These vapours and gases
came in to separator where heavy oil fraction was separated
from gases and the gases were passed through the series of
heat exchangers to condense the vapour into liquid form,
called tyre oil (40 to 45%) by means of recirculated water
from cooling tower and is collected into the storage tank. Non
condensable gases also called Pyro gases (about 10%) were
used for heating the reactor in place of oil, initially used for
heating purpose as per the requirement and the rest of the
gases were burnt in the open air by means of gas burner.
During the process carbon black (30 to 35%) and steel wires
(10 to 15%) were also generated.
B. Fuel Composition and Properties
Tyre oil derived from pyrolysis process was tested in the
laboratory for determination of its Physio-chemical properties
as compared to standard values for diesel as shown in the table
1. The liquids obtained are dark brown colored products,
resembling petroleum fractions.
Table I
Comparison of Properties of TPO with standard value for Diesel
SR.
NO
.
SPECIFICATION
S
UNITS TEST
RESULTS
STANDARD
VALUE OF
DIESEL
(IS:1460)
1 KINEMATIC
VISCOSITY AT
40O
C
cSt 8.65 2.0 - 4.5
2 ACIDITY,
INORGANIC
mgKOH/
gm
0.14 NIL
3 ASH % by
mass
0.04 0.01 MAX
4 FLASH POINT,
ABLES/PMCC
o
C 32 35MIN/
66MIN
5 WATER
CONTENT
mg/kg NIL 200 MAX
6 POUR POINT o
C +6 3 Min
7 DENSITY AT
15O
C
kg/cm3
0.910 0.820-0.845
8 SEDIMENTS Mg/100
ml
NIL ---
9 TOTAL
SULPHUR
mg/kg 88 50 MAX
10 CARBON
RESIDUE,
RAMSBOTTOM
% 0.85 0.30 MAX
11 COPPER STRIP
CORROSION
TEST FOR 3
HRS AT 100O
C
--- 1a <1
12 DISTILATION,
RECOVERY OF
95% AT O
C
O
C 390 360 MAX
13 COLOUR
INDEX
--- DARK TO REPORT
14 CETANE
NUMBER,
DIESEL INDEX
--- 42 51 MIN.
15 ACIDITY,
TOTAL
mgKOH/
gm
NIL TO REPORT
16 POLYCYCLIC
AROMATIC
HYDROCARBO
N
% by
mass
24 11
International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169
Volume: 6 Issue: 6 57- 62
______________________________________________________________________________________
59
IJRITCC | June 2018, Available @ http://www.ijritcc.org
______________________________________________________________________________________
Hence pyrolysis of scrap tyres produces oil that can be used as
liquid fuel for industrial furnaces, foundries and boilers in
power plants due to their higher calorific value, low ash, and
moisture content as far as sulphur content of oil is not a
problem. However, higher density, Kinematic viscosity and
Lower Cetane number of tyre oil suggest that the behaviour of
tyre oil in Internal Combustion Engine can be studied by
improving its quality in terms of reduction in density, viscosity,
sulphur and aromatic contents by proper distillation and
processing of tyre oil, if tyre oil is to be used as a fuel in
Internal Combustion Engine.
C. Refining tyre oil
Fractional distillation of tyre oil was carried out in the
boiling range of diesel in a distillation apparatus shown in
figure 2 in which a flask containing tyre oil was heated by
means of heating mental in the temperature range of
1500C to 3700C. The vapours formed were cooled by
means of circulating water in an inclined condenser and
condensed oil was collected in a measuring cylinder.
Collected oil was mixed with concentrated hydro sulphuric
acid on a volumetric basis in suitable proportion to reduce
sulphur and aromatic content of oil. The oil was then
neutralized and filtered by means of fine filter paper and
stored in a plastic container. The refined oil was tested in
the laboratory for determination of its Physio-chemical
properties as compared to standard values for diesel as
shown in the table 2
Fig. 2 Distillation Apparatus
Table II
Comparison of Properties of Refined TPO with standard value for Diesel
SR.
NO
.
SPECIFICATION
S
UNITS TEST
RESULTS
STANDARD
VALUE OF
DIESEL (IS:1460)
1 KINEMATIC
VISCOSITY AT
40O
C
cSt 2.30 2.0 - 4.5
2 ACIDITY,
INORGANIC
mgKOH
/gm
NIL NIL
3 ASH % by mass 0.01 0.01 MAX
4 FLASH POINT,
ABLES/PMCC
o
C <30 35MIN/
66MIN..
5 WATER
CONTENT
mg/kg NIL 200 MAX
6 POUR POINT o
C +3 3 Min
7 DENSITY AT 15O
C
kg/cm3
0.820 0.820-0.845
8 SEDIMENTS Mg/100ml NIL ---
9 TOTAL
SULPHUR
mg/kg 0.35 50 MAX
10 CARBON
RESIDUE,
RAMSBOTTOM
% 0.25 0.30 MAX
11 COPPER STRIP
CORROSION
TEST FOR 3 HRS
AT 100O
C
--- 1a <1
12 DISTILATION,
RECOVERY OF
92% AT O
C
O
C 360 360 MAX
13 COLOUR INDEX --- 5 TO REPORT
14 CETEN
NUMBER,
DIESEL INDEX
--- 44 51 MIN.
15 ACIDITY,
TOTAL
mgKOH
/gm
NIL TO REPORT
16 POLYCYCLIC
AROMATIC
HYDROCARBO
N
% by mass 7 11
International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169
Volume: 6 Issue: 6 57- 62
______________________________________________________________________________________
60
IJRITCC | June 2018, Available @ http://www.ijritcc.org
______________________________________________________________________________________
From the table it is clear that almost all the properties of
refined tyre oil are more or less within permissible limit of
Euro IV diesel specifications except flash point and Cetane
number, which suggests that the behavior of tyre oil in Internal
Combustion Engine can be studied through blending Tyre oil
with DF on volume basis. In the present work 10 %, 15%, and
20%, of TPO is blended with DF on a volume basis and
observed for 15 days to check for any separation. No such
separation was noticed. TPO blended with DF is indicated as
TPO xx. For example, the 10 % TPO blended with 90 % DF is
denoted as TPO 10.
III. EXPERIMENTAL DETAILS
In the present work single cylinder water cooled diesel engines
as shown in figure 3 is used for studying the performance and
emission characteristics of the TPO - DF blend at a crank
angle of 260
before TDC injection timing and 200 bar injection
pressure. The specifications of the engine are shown in table 3.
The fuel flow rate was measured on a volumetric basis using a
burette and a stop watch. The air flow rate was measured by
connecting the air intake to a large rigid box with an orifice at
its inlet to damp out pulsations in flow and by measuring the
pressure drop across orifice by means of the water tube
manometer.
Fig. 3 Single Cylinder Diesel Engine Test rig
Table III
Engine Details
Name of the Engine Captain
General Details Four stroke, CI, Water cooled, Single
Cylinder
Rated Power kw/bhp 3.7/5.0
Rated Speed(rpm) 1500
Bore(mm) 87.5
Stroke(mm) 110
Compression Ratio 16.5:1
Dynamometer Eddy current, water cooled with
loading unit
Fuel oil HSD
Lubricant SAE 30/40
Thermocouple with K type probe having temperature range 0-
1200o
C and accuracy 0.4% of the reading above 0o
C in
conjunction with a digital temperature indicator was used to
measure the exhaust gas and cooling water temperature.
Whereas sling Psychrometer was used to measure dry bulb
and wet bulb temperature of the surrounding. Laser photo
tachometer having 5 digits, 10 mm LCD display and range 10
to 99,999 RPM with accuracy ±0. 05% + 1 digit was used for
speed measurement. A Non dispersive Infrared 4-gas analyzer
was used to measure emissions in the exhaust. CO was
measured in percentage volume. HC was measured in ppm
volume. Smoke opacity was measured using a diesel smoke
meter. All the tests were conducted by starting the engine with
DF only. After the engine was warmed up, it was then
switched to TPO-DF blend. 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.
IV.RESULTS AND DISCUSSIONS
A. Performance Characteristics
I Brake Thermal Efficiency:
Fig. 4 Variations in Brake Thermal Efficiency with Brake Power
Figure.4 shows variation in Brake thermal efficiency with
Brake power. It maybe determined from the figure that the
thermal efficiency of TPO 10, TPO 15 and TPO 20 is lower
than that of diesel fuel (DF). This may be due to lower
viscosity of TPO which results in improper penetration of fuel
spray into the combustion chamber and inferior combustion.
II Specific Energy Consumption:
Figure.5 shows variation in Specific energy consumption with
Brake power. It may be determined from the figure that
specific energy consumption is higher for TPO 10, TPO 15
and TPO 20 as compared to Diesel fuel. This may be due to
lower calorific value of the TPO - DF blend as compared to
Diesel fuel.
International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169
Volume: 6 Issue: 6 57- 62
______________________________________________________________________________________
61
IJRITCC | June 2018, Available @ http://www.ijritcc.org
______________________________________________________________________________________
Fig. 5 Variations in Specific Energy Consumption with Brake Power
III Exhaust Gas Temperature:
Fig. 6 Variations in Exhaust Gas Temperature with Brake Power
Figure.6 shows variation in Exhaust gas temperature with
Brake power. It may be determined from the figure that the
exhaust gas temperature is more or less same or less than that
of diesel fuel. This may be due to better atomization and
vapourization of TPO due to lower viscosity.
B. Emission Characteristics
I Carbon Monoxide:
Figure.7 shows variation in Carbon Monoxide emission with
Brake power. It may be determined from the figure that CO
emission for TPO 10, TPO 15 and TPO 20 varies from 0.04 to
0.07 % which is slightly higher than that of diesel fuel but
Fig. 7 Variations in Carbon Monoxide emission with Brake Power
well below Euro IV emission requirement. This may be due to
rich air-fuel mixture at partial loads and volatility of TPO.
II Hydro Carbon:
Figure.8 shows variation in hydrocarbon emission with brake
power. It may be determined from the figure that hydrocarbon
emission is higher for TPO 10, TPO 15 and TPO 20 as
compared to diesel fuel.
Fig. 8 Variations in Hydro Carbon with Brake Power
This may be due to unsaturated hydrocarbons present in TPO
which are unbreakable during the combustion process [6]
as
well as higher aromatic content of tyre pyrolysis oil.
III Smoke Opacity:
Fig. 9 Variations in Smoke Opacity with Brake Power
International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169
Volume: 6 Issue: 6 57- 62
______________________________________________________________________________________
62
IJRITCC | June 2018, Available @ http://www.ijritcc.org
______________________________________________________________________________________
Figure.9 shows variation in smoke opacity with Brake power.
It may be determined from the figure that smoke opacity is
lower for TPO 10, TPO 15 and TPO 20 as compared to diesel
fuel. This may be due to finer fuel spray as well as higher
temperatures during the expansion stroke and more time for
oxidation of soot particles.
V. CONCLUSIONS
Based on the experimental investigations conducted on a
single cylinder diesel engine using TPO-DF blend, the
following major conclusions are observed.
[1] Brake thermal efficiency of the TPO - DF blend
is 6 to 10 % less than that of diesel fuel.
[2] CO emission is well below the permissible limit
for diesel engines.
[3] HC emission is higher by about 25 to 35% of the
TPO - DF blend as compared to DF for partial
load, but for a full load as well as overload
conditions it is more or less same as DF.
[4] Smoke opacity is lesser by about 03 to 21% of
the TPO - DF blend as compared to DF.
REFERENCES
[1] Cunnliffe. A.M., Williams. P.T. “Composition of oil
derived from the batch pyrolysis of tyres”, Journal of
Analytical and Applied Pyrolysis 44, October 1997,
pp.131-152.
[2] Roy C., Chaala A. and Darmstadt H “The Vacuum
Pyrolysis of Used Tyres End use of oil and carbon black
product”, Journal of Analytical and Applied Pyrolysis 51,
November 1998, pp. 201-221.
[3] Rodriguez I.M, Laresgoiti M.F, “Pyrolysis of scrap tyres”,
Fuel Processing Technology 72,February 2001, pp. 9-22
[4] Ucar S, Karagoz S, Ozkan A.R, and Yanik J, “Evaluation
of two different scarp tyres as hydrocarbon source by
pyrolysis," Fuel, vol. 84, 2005, pp. 1884-1892,
[5] Merchant, Petrich M.A, "Pyrolysis of scrap tyres and
conversion of chars to activated carbon," AIChE Journal,
vol. 39, 1993, pp. 1370-1376
[6] [6] Eco Energy Solutions, “Power Generation by
Scrap Tyres”, January 2011,
http://ecoenergysolutions.co.in/pdf/Pre project Report for
Waste Tyre to Energy. PDF (f)
[7] [7] Tamilvendhen D, Ilangovan V, Karthikeyan R,
"Optimization of engine operating parameters for
Eucalyptus oil mixed diesel fueled D I Diesel engine using
Taguchi Method" ARPN Journal of Engineering and
Applied Sciences, vol. 6, NO. 6, June 2011.
[8] [8] Nagarajan G, Rao A.N, Renganarayanan S,
“Emission and performance characteristics of neat ethanol
fuelled DI diesel engine” International Journal of Ambient
Energy., 2002, pp 149-158.

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Effect of Tyre Pyrolysis Oil (TPO) Blends on Performance of Single Cylinder Diesel Engine

  • 1. International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169 Volume: 6 Issue: 6 57- 62 ______________________________________________________________________________________ 57 IJRITCC | June 2018, Available @ http://www.ijritcc.org ______________________________________________________________________________________ Effect of Tyre Pyrolysis Oil (TPO) Blends on Performance of Single Cylinder Diesel Engine P M bhatt Mechanical Department, Gujarat technological University Government Polytechnic, Ahmedabad, Gujarat, India pmbhatt009@gmail.com Abstract— Increasing industrialization and motorization led to a significant rise in demand of petroleum products. As these are the non- renewable resources, it will be troublesome to predict the availability of these resources in the future, resulting in uncertainty in its supply and price and is impacting growing economies like India importing 80% of the total demand of the petroleum products. Many attempts have been made by different researchers to find out alternate fuels for Internal Combustion engines. Many alternate fuels like Biodiesel, LPG (Liquefied Petroleum Gas), CNG (Compressed Natural Gas) and Alcohol are being used nowadays by different vehicles. In this context pyrolysis of scrap tyres can be used effectively to produce oil, thereby solving the problem of waste tyre disposal. In the present study, Experimental investigations were carried out to evaluate the performance and emission characteristics of a single cylinder diesel engine fueled by TPO10, TPO15, and TPO20 at a crank angle 260 before TDC (Top Dead Centre) and injection pressure of 200 bar keeping the blend quality by controlling the density and viscosity of tyre pyrolysis oil within permissible limit of euro IV diesel requirement. The performance and emission results were analyzed and compared with that of diesel fuel operation. The results of investigations indicate that the brake thermal efficiency of the TPO - DF blend decreases by 6 to 10%. CO emissions are slightly higher but well within permissible limit of euro IV emission standards. HC emissions are higher by about 25 to 35% at partial load whereas smoke opacity is lower by about 3% to 21% as compared to diesel fuel. Keywords— Experimental Investigation, Diesel Engine, Tyre Pyrolysis Oil (TPO), Performance, Emission __________________________________________________*****_________________________________________________ I. INTRODUCTION Petroleum based fuels are stored fuels in the earth. There are limited reserves of these stored fuels and they are irreplaceable. This finite resource of petroleum are highly concentrated in certain regions of the world, have given rise to uncertainty in its supply and price and is impacting growing economies like India, importing 80% of the total demand of crude. India’s petroleum product consumption has increased from 100.4 million tonnes in 2001-02 to 133.4 million tonnes in 2008-09 at a CAGR of 4.1% and is likely to increase up to 217 million tonnes by 2020-21 and 325.6 million tonnes by 2030-31. All over the world, there are initiatives to replace gasoline and diesel fuel due to the impact of the fossil fuel crisis and hike in oil price. Millions of dollars are being invested in the search for alternative fuels. On the other hand, the disposal of waste tyres from automotive vehicles is becoming more and more complex. Waste to energy is the recent trend in the selection of alternate fuels. Fuels like alcohol, biodiesel, liquid fuel from plastics, etc. are some of the alternative fuels for the internal combustion engines. In order to prevent waste rubber and in particular discarded automobile tyres from damaging the environment, it is highly desirable to recycle this material in a useful manner. However, the total quantity of tyres currently recycled in a given year (excluding reuse, retreading, or combustion) is less than 7% of the annual tyre generation rate in the world. The use of tyre pyrolysis oil as a substitution of diesel fuel is an opportunity in minimizing the utilization of the natural resources. Several research works have been carried out on the pyrolysis of waste automobile tyres. Pyrolysis is the process of thermally degrading a substance into smaller, less complex molecules. Pyrolysis produces three principle products: such as pyrolytic oil, gas and char. The quality and quantity of these products depend upon the reactor temperature and design. In the Pyrolysis process, larger hydrocarbon chains break down at certain temperatures in the absence or a limited supply of oxygen that gives end products usually containing solids, liquids and gases. If the temperature is maintained at 550 ºC, the main product is a liquid, which could be a mixture of various hydrocarbons depending on the initial composition of the waste material. At temperatures above 700 ºC, the gas becomes the primary product due to further cracking of liquids. The gas is basically composed of CH4, with C2H6, C2H4, C2H2, and other gaseous hydrocarbons however in lesser quantities. In the present work pyrolysis oil from waste tyres by pyrolysis is obtained and used as a blended fuel in stationary diesel engine. Though solid carbon black and pyrolysis gas are also obtained, the pyrolysis process will be much more prominent to produce liquid [1, 2, 3, 4, and 5]. II. PREPARATION AND TESTING OF TYRE OIL A. Pyrolysis of Waste Automobile Tyres
  • 2. International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169 Volume: 6 Issue: 6 57- 62 ______________________________________________________________________________________ 58 IJRITCC | June 2018, Available @ http://www.ijritcc.org ______________________________________________________________________________________ Fig. 1 Waste Tyre Recycling Pyrolysis Plant Pyrolysis is a Thermo chemical decomposition of organic material at elevated temperature in the absence of oxygen. Pyrolysis typically occurs under pressure and at operating temperatures about 4300 C in a batch process system. In the present work waste automobile tyres were fed into 5Tonnes capacity rotary horizontal direct heating reactor vessel as shown in figure 1. Initially the heat was supplied by means of oil under controlled conditions of temperature and pressure. The process resulted in molecular restructuring of rubber and converted into vapours and gases. These vapours and gases came in to separator where heavy oil fraction was separated from gases and the gases were passed through the series of heat exchangers to condense the vapour into liquid form, called tyre oil (40 to 45%) by means of recirculated water from cooling tower and is collected into the storage tank. Non condensable gases also called Pyro gases (about 10%) were used for heating the reactor in place of oil, initially used for heating purpose as per the requirement and the rest of the gases were burnt in the open air by means of gas burner. During the process carbon black (30 to 35%) and steel wires (10 to 15%) were also generated. B. Fuel Composition and Properties Tyre oil derived from pyrolysis process was tested in the laboratory for determination of its Physio-chemical properties as compared to standard values for diesel as shown in the table 1. The liquids obtained are dark brown colored products, resembling petroleum fractions. Table I Comparison of Properties of TPO with standard value for Diesel SR. NO . SPECIFICATION S UNITS TEST RESULTS STANDARD VALUE OF DIESEL (IS:1460) 1 KINEMATIC VISCOSITY AT 40O C cSt 8.65 2.0 - 4.5 2 ACIDITY, INORGANIC mgKOH/ gm 0.14 NIL 3 ASH % by mass 0.04 0.01 MAX 4 FLASH POINT, ABLES/PMCC o C 32 35MIN/ 66MIN 5 WATER CONTENT mg/kg NIL 200 MAX 6 POUR POINT o C +6 3 Min 7 DENSITY AT 15O C kg/cm3 0.910 0.820-0.845 8 SEDIMENTS Mg/100 ml NIL --- 9 TOTAL SULPHUR mg/kg 88 50 MAX 10 CARBON RESIDUE, RAMSBOTTOM % 0.85 0.30 MAX 11 COPPER STRIP CORROSION TEST FOR 3 HRS AT 100O C --- 1a <1 12 DISTILATION, RECOVERY OF 95% AT O C O C 390 360 MAX 13 COLOUR INDEX --- DARK TO REPORT 14 CETANE NUMBER, DIESEL INDEX --- 42 51 MIN. 15 ACIDITY, TOTAL mgKOH/ gm NIL TO REPORT 16 POLYCYCLIC AROMATIC HYDROCARBO N % by mass 24 11
  • 3. International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169 Volume: 6 Issue: 6 57- 62 ______________________________________________________________________________________ 59 IJRITCC | June 2018, Available @ http://www.ijritcc.org ______________________________________________________________________________________ Hence pyrolysis of scrap tyres produces oil that can be used as liquid fuel for industrial furnaces, foundries and boilers in power plants due to their higher calorific value, low ash, and moisture content as far as sulphur content of oil is not a problem. However, higher density, Kinematic viscosity and Lower Cetane number of tyre oil suggest that the behaviour of tyre oil in Internal Combustion Engine can be studied by improving its quality in terms of reduction in density, viscosity, sulphur and aromatic contents by proper distillation and processing of tyre oil, if tyre oil is to be used as a fuel in Internal Combustion Engine. C. Refining tyre oil Fractional distillation of tyre oil was carried out in the boiling range of diesel in a distillation apparatus shown in figure 2 in which a flask containing tyre oil was heated by means of heating mental in the temperature range of 1500C to 3700C. The vapours formed were cooled by means of circulating water in an inclined condenser and condensed oil was collected in a measuring cylinder. Collected oil was mixed with concentrated hydro sulphuric acid on a volumetric basis in suitable proportion to reduce sulphur and aromatic content of oil. The oil was then neutralized and filtered by means of fine filter paper and stored in a plastic container. The refined oil was tested in the laboratory for determination of its Physio-chemical properties as compared to standard values for diesel as shown in the table 2 Fig. 2 Distillation Apparatus Table II Comparison of Properties of Refined TPO with standard value for Diesel SR. NO . SPECIFICATION S UNITS TEST RESULTS STANDARD VALUE OF DIESEL (IS:1460) 1 KINEMATIC VISCOSITY AT 40O C cSt 2.30 2.0 - 4.5 2 ACIDITY, INORGANIC mgKOH /gm NIL NIL 3 ASH % by mass 0.01 0.01 MAX 4 FLASH POINT, ABLES/PMCC o C <30 35MIN/ 66MIN.. 5 WATER CONTENT mg/kg NIL 200 MAX 6 POUR POINT o C +3 3 Min 7 DENSITY AT 15O C kg/cm3 0.820 0.820-0.845 8 SEDIMENTS Mg/100ml NIL --- 9 TOTAL SULPHUR mg/kg 0.35 50 MAX 10 CARBON RESIDUE, RAMSBOTTOM % 0.25 0.30 MAX 11 COPPER STRIP CORROSION TEST FOR 3 HRS AT 100O C --- 1a <1 12 DISTILATION, RECOVERY OF 92% AT O C O C 360 360 MAX 13 COLOUR INDEX --- 5 TO REPORT 14 CETEN NUMBER, DIESEL INDEX --- 44 51 MIN. 15 ACIDITY, TOTAL mgKOH /gm NIL TO REPORT 16 POLYCYCLIC AROMATIC HYDROCARBO N % by mass 7 11
  • 4. International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169 Volume: 6 Issue: 6 57- 62 ______________________________________________________________________________________ 60 IJRITCC | June 2018, Available @ http://www.ijritcc.org ______________________________________________________________________________________ From the table it is clear that almost all the properties of refined tyre oil are more or less within permissible limit of Euro IV diesel specifications except flash point and Cetane number, which suggests that the behavior of tyre oil in Internal Combustion Engine can be studied through blending Tyre oil with DF on volume basis. In the present work 10 %, 15%, and 20%, of TPO is blended with DF on a volume basis and observed for 15 days to check for any separation. No such separation was noticed. TPO blended with DF is indicated as TPO xx. For example, the 10 % TPO blended with 90 % DF is denoted as TPO 10. III. EXPERIMENTAL DETAILS In the present work single cylinder water cooled diesel engines as shown in figure 3 is used for studying the performance and emission characteristics of the TPO - DF blend at a crank angle of 260 before TDC injection timing and 200 bar injection pressure. The specifications of the engine are shown in table 3. The fuel flow rate was measured on a volumetric basis using a burette and a stop watch. The air flow rate was measured by connecting the air intake to a large rigid box with an orifice at its inlet to damp out pulsations in flow and by measuring the pressure drop across orifice by means of the water tube manometer. Fig. 3 Single Cylinder Diesel Engine Test rig Table III Engine Details Name of the Engine Captain General Details Four stroke, CI, Water cooled, Single Cylinder Rated Power kw/bhp 3.7/5.0 Rated Speed(rpm) 1500 Bore(mm) 87.5 Stroke(mm) 110 Compression Ratio 16.5:1 Dynamometer Eddy current, water cooled with loading unit Fuel oil HSD Lubricant SAE 30/40 Thermocouple with K type probe having temperature range 0- 1200o C and accuracy 0.4% of the reading above 0o C in conjunction with a digital temperature indicator was used to measure the exhaust gas and cooling water temperature. Whereas sling Psychrometer was used to measure dry bulb and wet bulb temperature of the surrounding. Laser photo tachometer having 5 digits, 10 mm LCD display and range 10 to 99,999 RPM with accuracy ±0. 05% + 1 digit was used for speed measurement. A Non dispersive Infrared 4-gas analyzer was used to measure emissions in the exhaust. CO was measured in percentage volume. HC was measured in ppm volume. Smoke opacity was measured using a diesel smoke meter. All the tests were conducted by starting the engine with DF only. After the engine was warmed up, it was then switched to TPO-DF blend. 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. IV.RESULTS AND DISCUSSIONS A. Performance Characteristics I Brake Thermal Efficiency: Fig. 4 Variations in Brake Thermal Efficiency with Brake Power Figure.4 shows variation in Brake thermal efficiency with Brake power. It maybe determined from the figure that the thermal efficiency of TPO 10, TPO 15 and TPO 20 is lower than that of diesel fuel (DF). This may be due to lower viscosity of TPO which results in improper penetration of fuel spray into the combustion chamber and inferior combustion. II Specific Energy Consumption: Figure.5 shows variation in Specific energy consumption with Brake power. It may be determined from the figure that specific energy consumption is higher for TPO 10, TPO 15 and TPO 20 as compared to Diesel fuel. This may be due to lower calorific value of the TPO - DF blend as compared to Diesel fuel.
  • 5. International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169 Volume: 6 Issue: 6 57- 62 ______________________________________________________________________________________ 61 IJRITCC | June 2018, Available @ http://www.ijritcc.org ______________________________________________________________________________________ Fig. 5 Variations in Specific Energy Consumption with Brake Power III Exhaust Gas Temperature: Fig. 6 Variations in Exhaust Gas Temperature with Brake Power Figure.6 shows variation in Exhaust gas temperature with Brake power. It may be determined from the figure that the exhaust gas temperature is more or less same or less than that of diesel fuel. This may be due to better atomization and vapourization of TPO due to lower viscosity. B. Emission Characteristics I Carbon Monoxide: Figure.7 shows variation in Carbon Monoxide emission with Brake power. It may be determined from the figure that CO emission for TPO 10, TPO 15 and TPO 20 varies from 0.04 to 0.07 % which is slightly higher than that of diesel fuel but Fig. 7 Variations in Carbon Monoxide emission with Brake Power well below Euro IV emission requirement. This may be due to rich air-fuel mixture at partial loads and volatility of TPO. II Hydro Carbon: Figure.8 shows variation in hydrocarbon emission with brake power. It may be determined from the figure that hydrocarbon emission is higher for TPO 10, TPO 15 and TPO 20 as compared to diesel fuel. Fig. 8 Variations in Hydro Carbon with Brake Power This may be due to unsaturated hydrocarbons present in TPO which are unbreakable during the combustion process [6] as well as higher aromatic content of tyre pyrolysis oil. III Smoke Opacity: Fig. 9 Variations in Smoke Opacity with Brake Power
  • 6. International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 2321-8169 Volume: 6 Issue: 6 57- 62 ______________________________________________________________________________________ 62 IJRITCC | June 2018, Available @ http://www.ijritcc.org ______________________________________________________________________________________ Figure.9 shows variation in smoke opacity with Brake power. It may be determined from the figure that smoke opacity is lower for TPO 10, TPO 15 and TPO 20 as compared to diesel fuel. This may be due to finer fuel spray as well as higher temperatures during the expansion stroke and more time for oxidation of soot particles. V. CONCLUSIONS Based on the experimental investigations conducted on a single cylinder diesel engine using TPO-DF blend, the following major conclusions are observed. [1] Brake thermal efficiency of the TPO - DF blend is 6 to 10 % less than that of diesel fuel. [2] CO emission is well below the permissible limit for diesel engines. [3] HC emission is higher by about 25 to 35% of the TPO - DF blend as compared to DF for partial load, but for a full load as well as overload conditions it is more or less same as DF. [4] Smoke opacity is lesser by about 03 to 21% of the TPO - DF blend as compared to DF. REFERENCES [1] Cunnliffe. A.M., Williams. P.T. “Composition of oil derived from the batch pyrolysis of tyres”, Journal of Analytical and Applied Pyrolysis 44, October 1997, pp.131-152. [2] Roy C., Chaala A. and Darmstadt H “The Vacuum Pyrolysis of Used Tyres End use of oil and carbon black product”, Journal of Analytical and Applied Pyrolysis 51, November 1998, pp. 201-221. [3] Rodriguez I.M, Laresgoiti M.F, “Pyrolysis of scrap tyres”, Fuel Processing Technology 72,February 2001, pp. 9-22 [4] Ucar S, Karagoz S, Ozkan A.R, and Yanik J, “Evaluation of two different scarp tyres as hydrocarbon source by pyrolysis," Fuel, vol. 84, 2005, pp. 1884-1892, [5] Merchant, Petrich M.A, "Pyrolysis of scrap tyres and conversion of chars to activated carbon," AIChE Journal, vol. 39, 1993, pp. 1370-1376 [6] [6] Eco Energy Solutions, “Power Generation by Scrap Tyres”, January 2011, http://ecoenergysolutions.co.in/pdf/Pre project Report for Waste Tyre to Energy. PDF (f) [7] [7] Tamilvendhen D, Ilangovan V, Karthikeyan R, "Optimization of engine operating parameters for Eucalyptus oil mixed diesel fueled D I Diesel engine using Taguchi Method" ARPN Journal of Engineering and Applied Sciences, vol. 6, NO. 6, June 2011. [8] [8] Nagarajan G, Rao A.N, Renganarayanan S, “Emission and performance characteristics of neat ethanol fuelled DI diesel engine” International Journal of Ambient Energy., 2002, pp 149-158.