Upload
mohsin-ehsan
View
18
Download
0
Embed Size (px)
Citation preview
1
Combustion(Lecture 3)
Lecture prepared for course in laserbased combustion diagnostics by Per-Erik Bengtsson and Joakim Bood
What is combustion?
Joakim Bood
Combustion takes place in a flame characterized by:
• Exothermic reactions – Reactants → Products + Energy
• Oxidation processes– Oxygen in air is usually the oxidizer
• High temperatures of the products– Typically above 2000 K
• Radiation – Chemiluminiscence, Planck radiation
2
Types of flames
Joakim Bood
Flat flameBunsen flame (followed by a nonpremixed candle for φ>1)
Wood fireCandle
Radiant burners for heatingLaminar
LaminarDiesel engineAircraft turbine
H2/O2 rocket engineTurbulentNonpremixed
(Diffusion)
Spark-Ignited gasoline enginesLow-NOx stationary gas turbineTurbulent
Premixed
ExamplesFluid motionFuel/oxidizer mixing
Premixed flames - Diffusion flames
Per-Erik Bengtsson and Joakim Bood
Fuel + air
Reaction zonePre-heat zone
Product zone
Porous-plug burnerUnburned gas zone
FuelAir Air
Fuel and air is mixed before combustion
Fuel and air burn when they meet
Premixed flames Nonpremixed flames(Diffusion flames)
3
Premixed flames
Joakim Bood
• Gaseous fuel and oxidizer are mixed on a molecular level prior to combustion
• Hydrocarbon/air flames have burning velocities around 0.5 m/s
Example: Spark-Ignition Engine
Nonpremixed flames (Diffusion flames)
Joakim Bood
• Fuel and oxidizer are introduced separately and mix during combustion
• Energy release rate limited by mixing process
• Reaction zone between oxidant and fuel zoneExample: Diesel Engine
4
Laminar flames
Joakim Bood
• Premixed– e.g. Bunsen flame– Rather low flame velocity
• Nonpremixed (Diffusion)– e.g. candle flame– Fuel: wax, Oxidizer: air– Reaction zone between
wax vapors and airPhoto: Per-ErikBengtsson
Photo: Per-Erik Bengtsson
v cold flow velocityα half the cone angleSL laminar flame speed
(the velocity of a reaction zoneorthogonal to its surface)
Bunsen flame structure
The flame is stationary, thus the following relation is valid:SL =v sinα
Reactionzone
SL is a property of a fuel/oxidant mixture at certain T and p, and it is around 0.5 m/s for hydrocarbon/air mixtures.
α
SL
v
x
© Per-Erik Bengtsson
Photo: Per-Erik Bengtsson
5
The reaction zone moves towards the unburned gas at velocity SL, mainly because H atoms diffuse towards the unburned gas and react with unburned oxygen
H + O2 OH + O
Zones of a premixed flame
Unburned gas zone Preheat zone Reaction zone Product zone
Temperature profile along x
300 K
~2000 K
x v sinα SL Radicals, such as H, OH, and O,are formedhere!
© Per-Erik Bengtsson
Photo: Per-Erik Bengtsson
Turbulent flames
Joakim Bood
• Premixed– Fast heat release– Increased flame propagation
rate– e.g. Spark-Ignition Engine
• Diffusion– Can obtain high rates of energy
release per unit volume– Modeling is very complex, no
well established approach– e.g. Diesel Engine
Photo: Per-Erik Bengtsson
Turbulent diffusion flame
6
Spark plug
Flamepropagation
Adiabatic assumptions
Joakim Bood
• No heat losses to the surroundings
• All heat produced by the combustion is available to heat the product gas
• Adiabatic flame temperature may be calculated
7
Adiabatic flame temperature
Joakim Bood
• Highest possible temperature that a flame can attain
• Never achieved in practice– No realistic combustion chamber is adiabatic– Dissociation of product lowers temperature
• Useful design parameter– Sets the upper temperature limit of the exhaust
Fuel Laminar flame speed Adiabatic flame[m/s] temperature [K]
AlkanesMethane/air 0.45 2225 Ethane/air 0.47 2260 Propane/air 0.46 2267
AlkenesEthene/air 0.75 2370Propene/air 0.72 2334
AlkynesEthyne/air 1.58 2539
Maximum laminar flame speed
© Per-Erik Bengtsson
8
Fuel + Air
Preheat zone
Reaction zone
Product zone
Sintered porous-plug
Flat flame on porous-plug burner
The flat premixed flame on a porous-plug burner is a proper research flame.
Each height represents a certain time in the combustion process.
The flame in the picture is very fuel-rich and soot is formed in the product zone.
© Per-Erik Bengtsson
Photo: Per-Erik Bengtsson
mixturetricstoichiomeinoxygenmolesfuelmoles
mixturerealinoxygenmolesfuelmoles
)#/(#
)/#(#=Φ
StoichiometryStoichiometry expresses the ratio between the fuel and oxidant concentration in a mixture.
The equivalence ratio, Φ, is used to specify this relationship:
The stoichiometric relation for propane combustion:
1 C3H8 + 5 O2 + 18.8 N2 → 3 CO2 + 4 H2O + 18.8 N2
Example: Calculate the equivalence ratio for a mixture with the molar ratio 1:4 between propane and oxygen:
2.15/1
4/1==Φ
© Per-Erik Bengtsson
9
Stoichiometry (2)
The mole fraction of propane:
Xpropane= 0.040 the mixture is stoichiometric
Xpropane< 0.040 the mixture is fuel-lean ⇒ O2 in the exhaust
Xpropane> 0.040 the mixture is fuel-rich ⇒ CO and H2 in the exhaust
040.08.1851
1=
++=propaneX
A stoichiometric hydrocarbon mixture gives a flame that ideally gives the products CO2 and H2O only. For such a flame Φ=1.
The stoichiometric relation for propane combustion:
1 C3H8 + 5 O2 + 18.8 N2 → 3 CO2 + 4 H2O + 18.8 N2
© Per-Erik Bengtsson
0% 20% 40% 60% 80% 100%
H2 + O2
H2 + air
CH4 + O2
CH4 + air
C2H6 + air
C3H8 + air
n-C4H10 + air
C2H2 + air
Fuel concentration in mixture
Flammability limits
It must be remembered that combustion is always a competition between heat-generating reactions and cooling processes!
© Per-Erik Bengtsson
10
Temperatures in flames
The highest temperature for a premixed hydrocarbon/air flameoften obtained at the slightly rich side of stoichiometric.
Temperature decreases when Φdecreases from around 1, since the heat released also must be used to heat up “surviving”oxygen and increasing amounts of nitrogen.
Temperature in ethane-air flames
0
500
1000
1500
2000
2500
0.6 0.7 0.8 0.9 1 1.1 1.2 1.3 1.4
Equivalence ratio
Tem
pera
ture
/ K
© Per-Erik Bengtsson
Major species concentrations in product gases
Concentrations in ethane-air flames
0
0,02
0,04
0,06
0,08
0,1
0,12
0,14
0,16
0,18
0.6 0.7 0.8 0.9 1 1.1 1.2 1.3 1.4
Equivalence ratio
Mol
e fr
actio
n
CO2
H2OWater and carbon dioxide have high concentrations over a large range of equivalence ratios.
© Per-Erik Bengtsson
11
Concentrations in ethane-air flame
0,00
0,01
0,02
0,03
0,04
0,05
0,06
0,07
0,08
0,09
0.6 0.7 0.8 0.9 1 1.1 1.2 1.3 1.4
Equivalence ratio
Mol
e fr
actio
n
O2
H2
CO
• Concentrations of CO and H2 increase when Φ is raised above 1.
• Concentration of O2increases when Φ is lowered below 1.
• At Φ =1 CO, H2, and O2have mole fraction above zero due to equilibrium considerations.
Species concentrations in product gases
© Per-Erik Bengtsson
Concentrations profiles across reaction zone (1)
Per-Erik Bengtsson
12
Concentrations across the reaction zone (2)
Per-Erik Bengtsson
Concentration distributions in diffusion flames
The figure illustrates the concentration distribution of major species in a diffusion flame on methane and air.
The figure illustrates the concentration distribution of additional species in a diffusion flame on methane and air.
Per-Erik Bengtsson
13
Combustion Chemistry (1)A global reaction is a reaction that shows the reactants and products. Howevernothing is said about how the reactionsoccur on a molecular level. An example is 2 H2 + 1 O2 2 H2O
The question is now how does the reactionbetween hydrogen and oxygen start?
H2+ M H + H + M
The hydrogen molecule and the other molecule must both have a very high energy, i.e. a high velocity, to create the first radicals.
The reaction starts from two molecules colliding and breaking apart. For example, H2 collides with another molecule in the gas, arbitrarily called M.
© Per-Erik Bengtsson
Combustion Chemistry (2)
Joakim Bood
Rates of chemical reactions
xAA + xBB + …. → xPP + xQQ + ….
Rate law:[ ] [ ] [ ] [ ] [ ] [ ]ba
QPBA
BAkdtQd
xdtPd
xdtBd
xdtAd
x===
−=
− 1111
Rate constanta: reaction order with respect to species Ab: reaction order with respect to species Ba + b: overall order of reaction
14
Combustion Chemistry (3)
Joakim Bood
Temperature dependence of the rate constant
RTEAk /exp−=
( )RTEAk /exp −= Arrhenius equation (two-parameter repr.)
A: Pre-exponential factor, E: Activation energy, R: ideal gas const, T: Temp
ExperimentCH4 + OH
Three-parameter Arrhenius expressionfitted to the measured data:
( )RTETAk n /exp' −=
Combustion chemistry (4)
A detailed chemical mechanism for hydrogen combustion contains 19 reactions.
Per-Erik Bengtsson & Joakim Bood
15
Combustion of methane:
1 CH4 + 2 O2 → 1 CO2 + 2 H2O
How does combustion proceed?
Methane oxidation mechanism:
Per-Erik Bengtsson
Full methane mechanism
149 reactions
Per-Erik Bengtsson
16
Summary: Premixed flames
Per-Erik Bengtsson
0
5E+10
1E+11
1.5E+11
2E+11
2.5E+11
3E+11
3.5E+11
4E+11
4.5E+11
400 800 1200 1600 2000 2400 2800
Wavelength (nm)
Sign
al in
tens
ity (W
/m3 )
T=1600KT=2000K
Visible spectral range
Planck radiation
© Per-Erik Bengtsson
Photo: Per-Erik Bengtsson
17
The blue-green emission from flames
The blue-green emission from the reaction zone has its origin in radicals that have been produced in an excited electronic state from chemical reactions, so-called chemi-luminescence.
CH contributes in the blue spectral region, and C2contributes in the blue and green spectral regions.
UV Visible
© Per-Erik Bengtsson