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Spray A Nozzle Tip Temperature Measurements Louis‐Marie Malbec, IFPEn Contributors: Lyle M. Pickett – Sandia National Laboratories Raul Payri, Julien Manin, Michele Bardi – CMT Motores Térmicos Tim Bazyn, Glen Martin – Caterpillar Maarten Meijer, L.M.T. Somers, Technische Universiteit Eindhoven Alan Kastengren, Argonne National Laboratories Summary of the workshop session: This session presented Spray A nozzle tip temperature measurements conducted at 6 contributing institutions: Sandia, IFPEn, CMT, Caterpillar, TUE and Argonne. As an introduction, the fact that it is impossible to measure the fuel right at the outlet of the injector was reminded. The measurement techniques and results shown in this presentation were thus attempts to access this fuel temperature as close as possible, through the measurement of the nozzle body temperature. The first part of the presentation described the different devices used by the contributing institutions, with an emphasis on the impact of the characteristics of the vessels on the fuel temperature:
• For continuous flow vessels (CMT, CAT) or cold flow vessels (Argonne), the vessel walls and ambient gas temperature are constant, so the injector is in steady state (no temporal evolution of its temperature).
• For preburn vessel, the ambient gas temperature is increasing during the combustion and then decreasing during the cool down process. The temperature of the injector and of the fuel is thus changing with time.
Besides, continuous flow vessels and preburn vessel require cooling systems to control the injector (in the cold flow vessel, the injector is heated). The geometry of these cooling systems and their ability to limit the heat rise may have an effect on the fuel temperature. At last, a ceramic cover is used to protect the nozzle tip from the ambient gas hot temperatures, and thus also to limit the temperature rise of the fuel. In the second part, the three different techniques used by the institutions to measure the nozzle tip temperature were presented. The first one consists in putting a thermocouple on the injector’s body, quite far from the nozzle tip. This type of measurement is relevant when the injector is in steady state and has been performed by CMT an Argonne. The second one, carried out at IFPEn, is based on the Laser Induced Phosphorescence (LIP), which allows the measurement of the temperature of the surface of the nozzle tip, and its evolution during the preburn event.
The last one requires the use of a dummy injector equipped with a K‐type thermocouple. This technique allows the measurement of the temperature within the sac volume, and gives access to its temporal and spatial evolution. At the moment of the workshop, only Sandia, TUE and CAT have used this dummy injector. In the third part, of the presentation, the results were analyzed. The temperature measured in the sac volume with the dummy injector is first compared between Sandia and TUE. This comparison shown great differences both in the amplitude of the temperature rise during the preburn, and of its evolution during the cool down event. But it is difficult to know whether these differences are due to variations in the efficiency of the ceramic shields, in the efficiency of the cooling systems or in the cool down behaviors. So no conclusion was drawn so far. The effect of the ceramic shield has also been investigated by IFPEn (LIP) and TUE (dummy injector). The results shown similar temperature evolutions, however at different levels, for theses two institutions, in spite of the different techniques used. The temperature of the surface of the nozzle tip seems thus to be strongly correlated with the sac volume temperature. Moreover, the ceramic shield used by TUE seems to be slightly more efficient than IFPEn one’s, as the temperature rise is higher at IFPEn. At last, the use of the dummy injector also allowed assessing the temperature gradients within the injector (Sandia, TUE, CAT). This showed a slight decrease of the temperature when the distance to the sac volume increases, but no conclusion can be drawn concerning the effect of such a gradient on the injected fuel temperature. As a conclusion, the difficulty to correlate the different temperature measurements with the real temperature of the injected fuel and its evolution was underlined. Recommendations:
• In order to assess and control the temperature of the injected fuel, the temperature must be measured in the sac volume.
• The dummy injector technique is the best one to access the sac volume temperature because of its simplicity (the post treatment is also quite easy) and of its accuracy.
• The use of a ceramic shield is a good way to limit the temperature rise of the sac volume. The design of TUE one’s seems to be the more efficient.
• When using a cooling system, people must be careful of the corrosion that can be induced by water condensation on the injector tip.
Discussion items from the workshop:
• As an answer to a question on the effect of the fuel temperature on liquid length, it was reminded that this was of first order, and thus needs to be controlled as precisely as possible.
• The modelers underlined that for the moment, there was no model able to take
into account the heat transfers between the fuel and the injector’s body within the nozzle hole. Thus, the temperature of the injected fuel right at the outlet of the injector can not be inferred from its temperature in the sac volume.
Renewable energies | Eco-friendly production | Innovative transport | Eco-efficient processes | Sustainable resources
Nozzle tip and injector's body temperature measurements
Spray A and hydraulic characterization
Gilles Bruneaux Louis-Marie MalbecGilles Bruneaux, Louis-Marie MalbecIFPEn
Lyle M. Pickett Raul Payri, Julien Manin, Michele Bardiy e c eSandia National Laboratories
au ay , Ju e a , c e e a dCMT Motorés Termicos
Tim BazinCaterpillar
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Alan KastengrenArgonne National Laboratories
Maarten Meijer, L.M.T SomersTechnische Universiteit Eindhoven
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IFPEN P b ti l ECN i tIFPEN Precombustion vessel ECN experiments
2009-2010Spray A
2011Multi points ambient temperature measurements: 5 thermocouplesmeasurements: 5 thermocouples probeNon reacting & reacting velocity fields: PIVSoot: LII + TEM
2012LIF formaldehyde + OH
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Lyle M. Pickett, Caroline L. Genzale, Gilles Bruneaux, Louis-Marie Malbec, Laurent Hermant, Caspar Christiansen, and Jesper Schramm, Comparison of Diesel Spray Combustion in Different High-Temperature, High-Pressure Facilities, SAE Int. J. Engines December 2010 3:156-181, SAE paper 2010-01-2106.
B G M li D St d f th Mi i d C b ti P f C ti Sh t D bl Di l
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Bruneaux, G., Maligne, D., Study of the Mixing and Combustion Processes of Consecutive Short Double Diesel Injections, SAE Int. J. Engines 2(1):1151-1169, 2009. (SAE 2009-01-1352)
Bruneaux, G., Combustion Structure of Free and Wall Impinging Diesel Jets by Simultaneous Laser Induced Fluorescence of Formaldehyde, PAH and OH, International Journal of Engine Research, volume 9, issue 3, 2008.
ContextContext
Behavior of the spray and characteristics of the combustion depend p y pon the temperature of the injected fuel.Fuel temperature is an input of the combustion models.
T t f S A diti f l i j t d t 90°C
=> Need for measuring and regulating the temperature of the injected fuel.
Target for Spray A conditions: fuel injected at 90°C.
90°C
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(open)
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ContextContext
Ideally we want to measure/controlIdeally, we want to measure/control the temperature:• of the fuel• just at the nozzle tipj p• during the whole injection
Needle
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ContextContext
Practically, we can measure the ytemperature:• of the injector body• at different locations• without injection and without fuel
Needle
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temperature of the injected fuel?
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injected fuel?
Institutions and facilitiesInstitutions and facilities
CMTCaterpillar
Temperature measurements are not time dependantCaterpillar
TUE (Eindhoven) Temperature measurementsSandia Nat. LabsIFPEn
Temperature measurements are time dependant
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ArgonneTemperature measurements are not time dependant, i j t i h t d
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injector is heated
Continuous flow vesselContinuous flow vessel
Heated wallsHeated walls=> the injector needs to be cooled
Constant and tunable temperature of the ambient air=> the injector's temperature is in steady state (except for
the effect of the fuel flow during injection)
CMT CAT
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Precombustion vessel
Heated walls
Precombustion vessel
Heated walls=> the injector needs to be cooled
A precomb is necessary to increase the temperature IFPEn Sandia TUE
within the vessel. Injection during the cooling of the gases.
=> the ambient air temperature is varying before injection: p y g jthe injector's temperature is not in a steady-state.
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Cold flow vesselCold flow vessel
Cold flowCold flow=> the injector needs to be heated
Constant temperature of the ambient air=> the injector's temperature is in steady state (except for
the effect of the fuel flow during injection)the effect of the fuel flow during injection)
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Institutions and facilitiesInstitutions and facilitiesCMT TUE Sandia
IFPEN CATCeramic shields
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Temperature measurement methodsTemperature measurement methodsThermocouple in dummy injector
CAT TUE Sandia
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K-type thermocouple(50 i )
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(50microns)
Temperature measurement methodsTemperature measurement methodsCMT TUE Sandia
IFPEN CAT
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Temperature measurement methodsTemperature measurement methodsLaser Induced Phosphorescence (LIP)
IFPENIFPEN
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Temperature measurement methodsTemperature measurement methodsCMT TUE Sandia
IFPEN CAT
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Temperature measurement methodsTemperature measurement methodsThermocouple on real injector
CMT
Continuous flow
CMT
vessel:Constant temp.
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T t
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Temperature sensor
ResultsResultsTransient temperature: TC in dummy injector, precomb. vessel (TUE Sandia)(TUE, Sandia)
110
120
130
re (degC)
TUE
Sandia •Amplitude is higher for Sandia’s vessel.
0 1 2 3 4 5 680
90
100
Temperatu
0 mmDistance to nozzle 2
•Temporal evolution is different
•Efficiency of the ceramic shield?
120
130
C)
TUE
Sandia
0 1 2 3 4 5 6Time ASI (s)
120
130
)
TUE
Sandia
Distance to nozzle 2mm •Efficiency of the cooling system?•Different cool down behaviour?
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90
100
110
Temperature (degC
1 mm90
100
110
Temperature (degC)
2
•Effect on injected fuel temperature?
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0 1 2 3 4 5 6 780
Time ASI (s)
1 mm0 1 2 3 4 5 6 7
70
80
Time ASI (s)
2 mm
ResultsResultsTransient temperature: cover effect
120
e (degC)
Sandia w/o cover
Sandia w cover
IFPEn
IFPEn20°C
100
mperature TUE w/o cover
TUE w cover10°C
20 C
60
80
surface tem Similar evolutions
Similar evolutions Ceramic shields allows to limit heat transfers towards the
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0 2 4 6 840
Ti ft i iti ( )
Nozzle
heat transfers towards the injector=> the control of the injected fuel temperature is more efficient
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Time after ignition (s) efficient.
ResultsResultsSteady state tip temperature
120
CAT 900K
CAT 850KThese results give an idea of the temperature gradients
80
100
ure (degC)
CAT 850K
CAT 950K
Sandia
TUE
of the temperature gradients within the injector.
=> Effect on injected fuel temperature?
60
80
Tem
peratu
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0 5 10 15 20 25 3040
Distance to nozzle (mm)
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Distance to nozzle (mm)
SynthesisSynthesis
Recommendations for the “best” experimental eco e da o s o e bes e pe e amethods
Use dummy injector to control the nozzle tip temperature at 90°C for spray A. Post-processing is quite easy.p y p g q yUse a ceramic shield to limit heat transfers towards injectorBe careful with low injector temperature (corrosion)
ModellingThe tip temperature and its evolution strongly depends on the experimental setup
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What is the real temperature of the injected fuel? We can assume an experimental uncertainty of about 30K.
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