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Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM -2014 
INTERNATIONAL JOURNAL OF MECHANICAL ENGINEERING 
17 – 19, July 2014, Mysore, Karnataka, India 
AND TECHNOLOGY (IJMET) 
ISSN 0976 – 6340 (Print) 
ISSN 0976 – 6359 (Online) 
Volume 5, Issue 9, September (2014), pp. 31-35 
© IAEME: www.iaeme.com/IJMET.asp 
Journal Impact Factor (2014): 7.5377 (Calculated by GISI) 
www.jifactor.com 
31 
 
IJMET 
© I A E M E 
AN EXPERIMENTAL STUDY ON KEROSENE BASED PULSE 
DETONATION ENGINE 
Vikram Athreya V1, N K S Rajan2, Manjunatha A3, H R Purushothama4 
1, 4(Department of Mechanical Engineering, Siddaganga Institute of Technology-Tumkur) 
2, 3(CGPL, Department of Aerospace Engineering, Indian Institute of Science, Bangalore) 
ABSTRACT 
The paper summarizes the experimental study on kerosene based pulse detonation engine in a tube for three 
different equivalence ratios. The kerosene was vaporized in a pre-evaporator before injected into combustion chamber. 
Pre-heated air was injected through a nozzle into the detonation tube. The charged tube was electrically ignited near the 
injector end. To enhance the DDT and to reduce the transition distance Shchelkin spiral was used inside the tube. 
Comparison of measured pressure at different locations of the tube with the CEA values were made that confirms to have 
crossed the CJ point and provide a stable detonation. 
KEYWORDS: Deflagration to Detonation transition (DDT), Equivalence ratio, Pulse Detonation Engine (PDE), Vapour 
kerosene. 
I. INTRODUCTION 
Every engine that is practically available in the industrial sector works on the deflagration combustion and this 
is known to have lower thermodynamic cycle efficiencies than those which work on detonation combustion [1]. Brophy 
et al. [2] showed that the theoretical thermal efficiencies for Chapman–Jouguet (CJ) detonation combustion and 
deflagration combustion are 56.4 and 36.3 % respectively. Fully constant volume combustion, corresponding to zero 
combustion time which is difficult to achieve since the combustion must be very rapid. Therefore, it is inferred that a 
pulse detonation engine (PDE) can offer better performance compared to current propulsion devices. Detonation can be 
initiated in many ways such as direct method, deflagration to detonation transition (DDT), etc. Practically detonation 
initiation using direct method will not be efficient since it requires high energy. The other method is via DDT which uses 
a low energy source to accelerate a flame to a detonation. The transition distance required to attain detonation in a tube is 
considered to be too high for the fuel/air mixtures. Reduction of transition distance is desirable for PDE applications with 
the added advantages of reduction of length and weight. Methods to promote DDT in shortening the distance are 
proposed using DDT enhancement devices. These methods include inserting regular or irregular obstacles such as a 
Shchelkin spiral, orifice plates, etc. 
Geraint Thomas et al. [3] carried studies on flame acceleration transition to detonation in a relatively long 
unobstructed piping system using different fuels like hydrogen, ethylene, methane, propane and acetone. The aim of the 
work was to obtain sufficient experimental data to predicting potential detonation flame acceleration and DDT in 
industrial process pipes. The result shows that for straight pipes, detonation was observed only in hydrogen–air and 
ethylene–air mixtures. Detonation was not observed with methane, propane or acetone as fuel.
Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM 
C. S. Wen et al. [4] worked on detonation initiation of JP 
-2014 
17 – 19, July 2014, Mysore, Karnataka, India 
PDE. The initiation of detonation of liquid fuel by vaporizing will increases its specific energy density and reduces its 
volume. For JP-8, the fully vaporized temperature ranges from 380 to 410 K. In this stu 
observed at a shorter distance for the mixture of fully vaporized JP 
413 K. 
The Chemical Equilibrium with Applications (CEA) [5] is a NASA’s Computer program that calculates 
chemical equilibrium compositions and properties of complex mixtures. The program is written in ANSI standard 
FORTRAN by Bonnie J. McBride and Sanford Gordon. CEA program uses CJ detonations model to get the pressure 
values which is used for validating the experimental values. 
In the present work, experiments were conducted to show the possibility of achieving the detonation with 
kerosene and air mixtures. Tests for three different equivalence ratios were carried out and the data’s were captured. The 
results shown are compared with theoretical values obtained from CEA. 
II. EXPERIMENTAL SETUP 
The experimental setup shown in fig. 1 consists of a kerosene evaporator, a pre 
detonation tube of 43mm internal diameter and associated mea 
oscilloscope, ignition electrodes, pulse generator, ignition transformer and pressure transducer PT1, PT2, and PT3 
mounted on tube at a distance 960 mm, 1090mm and 1210mm from igniter. Nitrogen was used to 
kerosene tank to prevent the vapour pressures do not lead to auto 
the kerosene was set to vary from 150°C to 220°C 
vaporization of the kerosene was complete, the heating was made just above vaporizing temperature and with a relatively 
larger residence time than that of its demand for the evaporation. To avoid the condensation of the fuel, air was pre 
heated to about 180°C before injected to the detonation tube. A Shchelkin spiral was inserted into the detonation tube to 
get enhanced DDT performance. 
At constant flow rates, derived from a pressurized fuel tank that was made to flow 
kerosene vapour from the outlet of evaporator was injected into the detonation tube through a nozzle. Specially calibrated 
rotameter was used to measure the flow rate of air through the tube. Hot air from the air pre 
detonation tube through the same nozzle and allowed to mix with kerosene 
The gaseous mixture of air and kerosene were injected into the detonation tube. Combustion was initiated at a 
distance of 140mm from the injection point through the pair of electrodes. Consequently it was observed that the 
combustion starts with deflagration and the flame propagates towards the open end. Compression waves would get 
formed in the propagating direction due to the acceleration of 
This compression wave accumulated to form a local explosion in the unburned gases ahead of the combustion wave and 
has led to successful transition that ends up as a detonation wave. The specially procu 
mounted at different locations along the tube length record the pressures in the tube with the help of signal conditioner 
and digital storage oscilloscope. 
32 
JP-8–oxygen mixtures at different initial temperatures in 
study, detonation initiation was 
JP-8 and oxygen when the initial temperature exceeded 
lts pre-heater for air, 2 m long 
measurement devices that include signal conditioner, 
auto-ignition of the kerosene. The vaporizing temperature of 
to meet its vaporization characteristics [6]. In order to ensur 
Fig. 1: Experimental setup 
into the evaporator and 
pre-heater was made 
vapour before the ignition. 
ection the combustion wave and expansion of the burned gas. 
procured high speed pressure transducers 
 
dy, surement pressurize the liquid 
ensure that 
pre-before 
to enter the 
red
Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM -2014 
17 – 19, July 2014, Mysore, Karnataka, India 
33 
III. RESULTS AND DISCUSSION 
 
CEA program provides theoretical pressure value of detonation using the CJ detonation model. The table 1 
shows the pressure value of detonation for different equivalence ratios predicted by CEA program. 
Table 1: CEA pressure values for three equivalence ratios 
Equivalence ratio () 1.14 1 0.89 
CEA values in bar 19.27 18.60 17.78 
The fig. 2 shown here gives the pressure-time record, captured from three transducers PT1, PT2, and PT3 
mounted on the detonation tube at designated lengths of the tube, for  = 1. The peak pressure recorded by PT1 was 
18.12 bar and the peak pressure recorded by PT2 was 26.17 bar. The observation indicate clearly that the compression 
waves were formed in the propagating direction due to acceleration of the combustion wave have resulted in the 
expansion of the burned gas as seen the raise in pressure across PT1 and PT2 and has resulted in the expected 
deflagration to detonation transition (DDT). The peak pressure at PT3 was found to be 9.4 bar indicating the drop in 
pressure across PT2 and PT3 representing the expansion process of exhaust gases. From the theoretical value of CJ point 
predicted from CEA for the detonation (see the table 1) and the experimental value, it clears that the DDT has well 
established in the PDE confirming the detonation before the point PT2 which was 1090mm or within about 25 times the 
diameter of the tube, measured from the ignition point. 
Fig. 2: Plot of Pressure v/s Time for  = 1 
The fig. 3 shows the record of pressure versus time plot for  = 1.14, the peak pressures observed at the 
transducers PT1 and PT2 were 14.76 and 24.83 bars respectively that confirms again a clear detonation before PT2 (see 
table 1 for the CJ point for this). The pressure at PT3 was decaying to 8.05 bar as also was observed in the earlier case 
indicating exhaust process of the engine.
Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM -2014 
17 – 19, July 2014, Mysore, Karnataka, India 
34 
 
Fig. 3: Plot of Pressure v/s Time for  = 1.14 
Fig. 4: Plot of Pressure v/s Time for  = 0.89
Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM -2014 
17 – 19, July 2014, Mysore, Karnataka, India 
35 
 
The fig. 4 shows the record of pressure versus time plot for  = 0.89, the pressure at PT1 and PT2 were 8.05 bar 
and 19.46 bar respectively. With reference to table 1, the experimental value at PT2 confirms to have the detonation 
occurred. The pressure at PT3 was 6.03 bar, consistent with the earlier explanations. 
The experiments were carried repeatedly for all the three equivalence ratios and results were captured. The table 
2 shows the comparison of CEA values with experimental values for three equivalence ratio. Each equivalence ratio 
shown confirms the detonation before the point PT2 which was 1090 mm about 25 times the diameter of the tube from 
the ignition point. 
Table 2: - Comparison of CEA values with experimental values for three equivalence ratio 
Equivalence ratio () CEA values in bar 
Experimental values in bar 
PT1 PT2 PT3 
1.14 19.27 
14.76 24.83 8.05 
13.42 24.12 8.72 
14.09 24.83 8.72 
1 18.60 
18.12 26.84 9.4 
17.47 25.50 8.72 
18.12 26.17 10.65 
0.89 17.78 
8.72 20.13 5.36 
8.05 19.46 6.03 
8.05 19.46 5.36 
IV. CONCLUSION 
The experiments have been conducted in a specially built PDE for kerosene and have been tested for successful 
functioning of it for three different equivalence ratios. Kerosene was heated just above its vaporizing temperature and air 
was pre-heated to about 180°C to ensure the fuel and air were in the condition of gaseous mix for a clean detonation to 
occur. Pressure transducers mounted on the detonation tube along with ignition source have enabled to capture the 
process of DDT clearly and observations were found to be very repeatable. The present work shows out a clear 
possibility of managing controlled detonation at the tested equivalence ratios and make path for extended study for 
building a PDE as possible futuristic high efficiency engines using storable fuels like kerosene and using ambient air for 
the combustion. 
V. REFERENCE 
[1] Vutthivithayarak R, Braun E.M, Lu F.K, “Examination of the various cycles for pulse detonation engines”. AIAA 
paper no. 6064. 
[2] Brophy C M, Netzer D W, Sinibaldi J, Johnson R, “Detonation of a JP-10 aerosol for pulse detonation 
applications” In Roy G.D, Frolov S.M, Netzer D.W, Borisov A.A, High Speed Deflagration and Detonation” 
Fundamentals and Control, pp. 207–222. 
[3] Geraint Thomas, Gwyn Oakley, Richard Bambrey, “An experimental study of flame acceleration and 
deflagration to detonation transition in representative process piping” (2010). 
[4] C. S. Wen, K M Chung, W H Lai, “Detonation initiation of JP-8–oxygen mixtures at different initial 
temperatures” (2012). 
[5] NASA CEA, “NASA Computer Program for calculation of Chemical Equilibrium with Applications”. 
[6] “Kerosene/Jet fuel category assessment document”, The American Petroleum Institution (2010).

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An experimental study on kerosene based pulse detonation engine

  • 1. Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM -2014 INTERNATIONAL JOURNAL OF MECHANICAL ENGINEERING 17 – 19, July 2014, Mysore, Karnataka, India AND TECHNOLOGY (IJMET) ISSN 0976 – 6340 (Print) ISSN 0976 – 6359 (Online) Volume 5, Issue 9, September (2014), pp. 31-35 © IAEME: www.iaeme.com/IJMET.asp Journal Impact Factor (2014): 7.5377 (Calculated by GISI) www.jifactor.com 31 IJMET © I A E M E AN EXPERIMENTAL STUDY ON KEROSENE BASED PULSE DETONATION ENGINE Vikram Athreya V1, N K S Rajan2, Manjunatha A3, H R Purushothama4 1, 4(Department of Mechanical Engineering, Siddaganga Institute of Technology-Tumkur) 2, 3(CGPL, Department of Aerospace Engineering, Indian Institute of Science, Bangalore) ABSTRACT The paper summarizes the experimental study on kerosene based pulse detonation engine in a tube for three different equivalence ratios. The kerosene was vaporized in a pre-evaporator before injected into combustion chamber. Pre-heated air was injected through a nozzle into the detonation tube. The charged tube was electrically ignited near the injector end. To enhance the DDT and to reduce the transition distance Shchelkin spiral was used inside the tube. Comparison of measured pressure at different locations of the tube with the CEA values were made that confirms to have crossed the CJ point and provide a stable detonation. KEYWORDS: Deflagration to Detonation transition (DDT), Equivalence ratio, Pulse Detonation Engine (PDE), Vapour kerosene. I. INTRODUCTION Every engine that is practically available in the industrial sector works on the deflagration combustion and this is known to have lower thermodynamic cycle efficiencies than those which work on detonation combustion [1]. Brophy et al. [2] showed that the theoretical thermal efficiencies for Chapman–Jouguet (CJ) detonation combustion and deflagration combustion are 56.4 and 36.3 % respectively. Fully constant volume combustion, corresponding to zero combustion time which is difficult to achieve since the combustion must be very rapid. Therefore, it is inferred that a pulse detonation engine (PDE) can offer better performance compared to current propulsion devices. Detonation can be initiated in many ways such as direct method, deflagration to detonation transition (DDT), etc. Practically detonation initiation using direct method will not be efficient since it requires high energy. The other method is via DDT which uses a low energy source to accelerate a flame to a detonation. The transition distance required to attain detonation in a tube is considered to be too high for the fuel/air mixtures. Reduction of transition distance is desirable for PDE applications with the added advantages of reduction of length and weight. Methods to promote DDT in shortening the distance are proposed using DDT enhancement devices. These methods include inserting regular or irregular obstacles such as a Shchelkin spiral, orifice plates, etc. Geraint Thomas et al. [3] carried studies on flame acceleration transition to detonation in a relatively long unobstructed piping system using different fuels like hydrogen, ethylene, methane, propane and acetone. The aim of the work was to obtain sufficient experimental data to predicting potential detonation flame acceleration and DDT in industrial process pipes. The result shows that for straight pipes, detonation was observed only in hydrogen–air and ethylene–air mixtures. Detonation was not observed with methane, propane or acetone as fuel.
  • 2. Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM C. S. Wen et al. [4] worked on detonation initiation of JP -2014 17 – 19, July 2014, Mysore, Karnataka, India PDE. The initiation of detonation of liquid fuel by vaporizing will increases its specific energy density and reduces its volume. For JP-8, the fully vaporized temperature ranges from 380 to 410 K. In this stu observed at a shorter distance for the mixture of fully vaporized JP 413 K. The Chemical Equilibrium with Applications (CEA) [5] is a NASA’s Computer program that calculates chemical equilibrium compositions and properties of complex mixtures. The program is written in ANSI standard FORTRAN by Bonnie J. McBride and Sanford Gordon. CEA program uses CJ detonations model to get the pressure values which is used for validating the experimental values. In the present work, experiments were conducted to show the possibility of achieving the detonation with kerosene and air mixtures. Tests for three different equivalence ratios were carried out and the data’s were captured. The results shown are compared with theoretical values obtained from CEA. II. EXPERIMENTAL SETUP The experimental setup shown in fig. 1 consists of a kerosene evaporator, a pre detonation tube of 43mm internal diameter and associated mea oscilloscope, ignition electrodes, pulse generator, ignition transformer and pressure transducer PT1, PT2, and PT3 mounted on tube at a distance 960 mm, 1090mm and 1210mm from igniter. Nitrogen was used to kerosene tank to prevent the vapour pressures do not lead to auto the kerosene was set to vary from 150°C to 220°C vaporization of the kerosene was complete, the heating was made just above vaporizing temperature and with a relatively larger residence time than that of its demand for the evaporation. To avoid the condensation of the fuel, air was pre heated to about 180°C before injected to the detonation tube. A Shchelkin spiral was inserted into the detonation tube to get enhanced DDT performance. At constant flow rates, derived from a pressurized fuel tank that was made to flow kerosene vapour from the outlet of evaporator was injected into the detonation tube through a nozzle. Specially calibrated rotameter was used to measure the flow rate of air through the tube. Hot air from the air pre detonation tube through the same nozzle and allowed to mix with kerosene The gaseous mixture of air and kerosene were injected into the detonation tube. Combustion was initiated at a distance of 140mm from the injection point through the pair of electrodes. Consequently it was observed that the combustion starts with deflagration and the flame propagates towards the open end. Compression waves would get formed in the propagating direction due to the acceleration of This compression wave accumulated to form a local explosion in the unburned gases ahead of the combustion wave and has led to successful transition that ends up as a detonation wave. The specially procu mounted at different locations along the tube length record the pressures in the tube with the help of signal conditioner and digital storage oscilloscope. 32 JP-8–oxygen mixtures at different initial temperatures in study, detonation initiation was JP-8 and oxygen when the initial temperature exceeded lts pre-heater for air, 2 m long measurement devices that include signal conditioner, auto-ignition of the kerosene. The vaporizing temperature of to meet its vaporization characteristics [6]. In order to ensur Fig. 1: Experimental setup into the evaporator and pre-heater was made vapour before the ignition. ection the combustion wave and expansion of the burned gas. procured high speed pressure transducers dy, surement pressurize the liquid ensure that pre-before to enter the red
  • 3. Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM -2014 17 – 19, July 2014, Mysore, Karnataka, India 33 III. RESULTS AND DISCUSSION CEA program provides theoretical pressure value of detonation using the CJ detonation model. The table 1 shows the pressure value of detonation for different equivalence ratios predicted by CEA program. Table 1: CEA pressure values for three equivalence ratios Equivalence ratio () 1.14 1 0.89 CEA values in bar 19.27 18.60 17.78 The fig. 2 shown here gives the pressure-time record, captured from three transducers PT1, PT2, and PT3 mounted on the detonation tube at designated lengths of the tube, for = 1. The peak pressure recorded by PT1 was 18.12 bar and the peak pressure recorded by PT2 was 26.17 bar. The observation indicate clearly that the compression waves were formed in the propagating direction due to acceleration of the combustion wave have resulted in the expansion of the burned gas as seen the raise in pressure across PT1 and PT2 and has resulted in the expected deflagration to detonation transition (DDT). The peak pressure at PT3 was found to be 9.4 bar indicating the drop in pressure across PT2 and PT3 representing the expansion process of exhaust gases. From the theoretical value of CJ point predicted from CEA for the detonation (see the table 1) and the experimental value, it clears that the DDT has well established in the PDE confirming the detonation before the point PT2 which was 1090mm or within about 25 times the diameter of the tube, measured from the ignition point. Fig. 2: Plot of Pressure v/s Time for = 1 The fig. 3 shows the record of pressure versus time plot for = 1.14, the peak pressures observed at the transducers PT1 and PT2 were 14.76 and 24.83 bars respectively that confirms again a clear detonation before PT2 (see table 1 for the CJ point for this). The pressure at PT3 was decaying to 8.05 bar as also was observed in the earlier case indicating exhaust process of the engine.
  • 4. Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM -2014 17 – 19, July 2014, Mysore, Karnataka, India 34 Fig. 3: Plot of Pressure v/s Time for = 1.14 Fig. 4: Plot of Pressure v/s Time for = 0.89
  • 5. Proceedings of the 2nd International Conference on Current Trends in Engineering and Management ICCTEM -2014 17 – 19, July 2014, Mysore, Karnataka, India 35 The fig. 4 shows the record of pressure versus time plot for = 0.89, the pressure at PT1 and PT2 were 8.05 bar and 19.46 bar respectively. With reference to table 1, the experimental value at PT2 confirms to have the detonation occurred. The pressure at PT3 was 6.03 bar, consistent with the earlier explanations. The experiments were carried repeatedly for all the three equivalence ratios and results were captured. The table 2 shows the comparison of CEA values with experimental values for three equivalence ratio. Each equivalence ratio shown confirms the detonation before the point PT2 which was 1090 mm about 25 times the diameter of the tube from the ignition point. Table 2: - Comparison of CEA values with experimental values for three equivalence ratio Equivalence ratio () CEA values in bar Experimental values in bar PT1 PT2 PT3 1.14 19.27 14.76 24.83 8.05 13.42 24.12 8.72 14.09 24.83 8.72 1 18.60 18.12 26.84 9.4 17.47 25.50 8.72 18.12 26.17 10.65 0.89 17.78 8.72 20.13 5.36 8.05 19.46 6.03 8.05 19.46 5.36 IV. CONCLUSION The experiments have been conducted in a specially built PDE for kerosene and have been tested for successful functioning of it for three different equivalence ratios. Kerosene was heated just above its vaporizing temperature and air was pre-heated to about 180°C to ensure the fuel and air were in the condition of gaseous mix for a clean detonation to occur. Pressure transducers mounted on the detonation tube along with ignition source have enabled to capture the process of DDT clearly and observations were found to be very repeatable. The present work shows out a clear possibility of managing controlled detonation at the tested equivalence ratios and make path for extended study for building a PDE as possible futuristic high efficiency engines using storable fuels like kerosene and using ambient air for the combustion. V. REFERENCE [1] Vutthivithayarak R, Braun E.M, Lu F.K, “Examination of the various cycles for pulse detonation engines”. AIAA paper no. 6064. [2] Brophy C M, Netzer D W, Sinibaldi J, Johnson R, “Detonation of a JP-10 aerosol for pulse detonation applications” In Roy G.D, Frolov S.M, Netzer D.W, Borisov A.A, High Speed Deflagration and Detonation” Fundamentals and Control, pp. 207–222. [3] Geraint Thomas, Gwyn Oakley, Richard Bambrey, “An experimental study of flame acceleration and deflagration to detonation transition in representative process piping” (2010). [4] C. S. Wen, K M Chung, W H Lai, “Detonation initiation of JP-8–oxygen mixtures at different initial temperatures” (2012). [5] NASA CEA, “NASA Computer Program for calculation of Chemical Equilibrium with Applications”. [6] “Kerosene/Jet fuel category assessment document”, The American Petroleum Institution (2010).