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Burners & Flame
 COMBUSTION REACTION
Combustion is a reaction between oxygen and fuel.
This oxidation is an exothermic reaction.
Correct proportion
OXYGEN FUEL
FLAME
Ignition
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Firing
2
 BURNERS
OBJECTIVE: Insert fuel in the burning zone.
Its efficiency depends on the speed it enters in contact with
oxygen. They should be planned and regulated by way of
setting the heat in the ideal place, by way of not causing
damages to the wall (refractory) and to produce as less
pollutants and possible (CO, NOx, SO2).
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Firing
Rotary Kiln Burner & Flame Theory
 Function of a rotary kiln burner:
• Mix fuel and combustion air to produce a stable flame and to release heat in a way adapted to process requirements.
 Diffusion flames:
• Burner fed with 100% of the kiln fuels but only ~10% of required combustion air (Primary Air). The other 90% of combustion
air comes from the cooler (Secondary Air), to recover the material energy. Thus, with only 10% of the combustion air, the
burner must be able to produce:
 An adjustable thermal profile
 A stable flame:
 Efficient combustion & Reduced air emissions
 Impulse (Momentum):
• Force generated by the primary air and fuels discharge
velocity at the burner tip.
 Impulse (N) = Mass flow (kg/s) x Velocity (m/s)
• It generates the secondary air and the fuels mixing.
• Proportional to the heat release: Specific Impulse (N/MW) C
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Peers Conference 2019 – Rotary Kiln Burner
 Single stage burners
Unique duct to:
Fuel + primary air
Usually used for short kiln. They can be used for fuel
simultaneously with other fuels, and in this case they have to
be equipped with an extra pipe in the centre of the duct.
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Coal and/or pet cock
Edição:0
Firing
 Multi-stage burners
For a more efficient adjustment in the flame, through
primary air, multi-stage burners are used, which are divided
in two components, axial and radial, with the fuel being
introduced also through a tube which is concentric with
others.
They can be used for only one fuel or for several alternately
or simultaneously (gas, liquid or solid).
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S axial
transport
swirl
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Firing
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Firing
Axial air is injected towards the kiln axel.
The swirl air is injected towards the kiln burner (the angle is
one of the burner’s project parameters) .
 Multi-stage burners
The swirl component of radial air creates a rotating air flow
around the kiln (like a screw), which also pushes in towards
the exterior.
As the swirl air is located internally to the axial air, its
increase causes flame enlargement.
 Pillard Rotaflam
 FLS Duoflex
 Unitherm M.A.S.
 Greco-Enfil / Flexiflame (new)
 KHD Pyrojet / Pyrostream
 Polysius Polflame
Burner Suppliers Overview
Most used burners in Holcim plants
42
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
MAIN BURNER
Lafarge
KHD
MAS Unitherm
Greco Pillard Rotaflam
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Firing
FLS Duoflex Burner – logical PA adjustments
 The sum of the axial and swirl air exit cross can be adjusted
 Only one fan for axial and swirl channel is used
 Burner momentum remains by changing axial/radial split
44
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
PYRO-JET Burner ®
Central air duct
Rotation air
Mud duct
Per cock duct
Axial air oil / solvents / water duct
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Edição:0
Firing
Fuel
Secondary air
Axial Air
Swirl air
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PYRO-JET Burner ®
Edição:0
Firing
+
+
Secondary air
Secondary air
Axial
Axial
Radial/Swirl
Radial/Swirl
Central
18
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
Primary air split up into Axial, Radial and Central Air
Primary air and multichannel burner tip
Axial air
Radial air
Nat. gas
Pulv. coal
Liquid &
Solid wastes
Axial air
Nat. gas
Radial air
Pulv. coal
Liquid &
Solid wastes
Coal
Natural gas
Cooling air
Radial Air
Axial air
Radial Air
Axial air
Coal
Natural gas
Cooling air
19
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
Pillard Rotaflam Burner – highest flexibility
 The cross sections of the axial, radial and coal channel can
be individually adjusted
 Good experience with the updated tip design RV2
 New “blowing device” for AFR channel
43
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
 Primary air ratio 13 – 15%
 Based on stoichiometric combustion air (Amin),
excluding transport air
Primary air fan pressure > 300 mbar
Main Burner Design Criteria
 Specific burner Impulsion (momentum) installed for
new multi-channel burners:
G = 11 N/MW

 Solid fuel injection velocities:
35…40 m/s
~30 m/s
~25 m/s
30…45 m/s



 Lignite
Coal
Petcoke
AFR
26
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
[N/MW]
%PA = percentage of primary air [%]
Primary air velocity (Bernoulli) :
ptip  pressure at burner inlet -5%
[m/s]
[Pa]
tip = air density at burner tip [kg/m3]
(T = 50°C, p = ambient pressure)
Example:
Amount of primary air: PA = 14%; pBurner Inlet = 300 mbar
 vPA = 233 m/s  G = 10.9 N/MW
Main Burner Design Criteria - Impulsion
G 
%PAvPA
300
Quick calculation of specific burner impulsion:
tip
28
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
PA
v 

2 ptip
 Primary air ratio 13 – 15%
Main Burner Design Criteria
 Specific burner Impulsion (momentum) installed for
new multi-channel burners:
G = 11 N/MW

 Based on stoichiometric combustion air (Amin),
excluding transport air
Primary air fan pressure > 300 mbar
 Solid fuel injection velocities:
35…40 m/s
~30 m/s
~25 m/s
30…45 m/s



 Lignite
Coal
Petcoke
AFR
30
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
Unitherm M.A.S. Burner – all adjustable swirl air
 Brings the whole primary air amount into swirl
 Single air jet penetration with several nozzles
 Continuous swirl adjustment between 0 - 40°
45
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
Unitherm Burner
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Firing
Allows to vary the swirl angle
Edição:01 Firing 170
Swirl Air
Axial Air
Pet coke
ASB
Animal Meal
Used oils
Central Ar
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02 Jan 2006
 LAFARGE BURNER
Independent ring jets, with
nebulization per auxiliary fluid
(compressed air or vapour); open
chamber type nozzle.
Burner with three adjustment air ducts.
Each ring for solid fuel and central duct
for the alternative solid fuel.
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GRECO Burner
Edição:0
Firing
DESIGN OF
FLEXIFLAME
BURNERS FOR
PETCOKE
2011
23
EXTERNAL AIR
TANGENTIAL AIR (ROTATION)
COAL/PETCOKE
DISPERSION AIR (ROTATION)
CENTRAL AIR
(RECIRCULATION/COOLING
SLUDGES / ANIMALMEAL
IGNITOR
MIXING AIR FOR ASF
RDF / FLUFF
DOUBLE SWIRL EFFECT
FLAME
CONTROL
2011
24
Fives Pillard
Rotaflam® Burner
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Peers Conference 2019 – Rotary Kiln Burner
Fives Pillard Rotaflam® Burner – Multichannel Burner
 Adjustable tips cross section during operation
 Independently adjustable primary air & natural gas
pressure & flowrates
2. Central stabilizer
 Improved flame stability (bluff body = internal recirculation)
 Possibility for integrated warm-up burner for gaseous or liquid
fuel
 Possibility for integrated igniter & flame detection
 Possibility for integrated lance for solid, liquid or gaseous fuels
3. Fuel concentration for NOx reduction
 Fuel injection inside primary air
 Low O2 content at flame core
 Rotaflam® Multichannel Burner
1. Adjustable Axial air, Radial air & Natural Gas tips
 Flame shaping:
HFO / NG / Biogas / NCG / Petcoke HFO / Methanol – Ignitor trial
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Peers Conference 2019 – Rotary Kiln Burner
Fives Pillard Rotaflam® Burner – Main Characteristics
 Coal / Petcoke /
Anthracite / Lignite
 Central stabilizer
• ASF / ALF / HFO / DO
• Ignitor / Flame detection
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Axial primary air
Adjustable cross section
 Radial primary air
Adjustable cross section
 Natural gas
Adjustable cross section
Peers Conference 2019 – Rotary Kiln Burner
Fives Pillard Rotaflam® Burner – Main Characteristics
Axial & Radial air pressure control
Axial air tip
adjustment
Radial air tip
adjustment
Natural gas Coal
Cooling air
Axial air
Radial air
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Peers Conference 2019 – Rotary Kiln Burner
Fives Pillard Rotaflam® Burner – Adjustable momentum principle
Axial tip: CLOSED (minimum section)
Air flowrate: REDUCED
Momentum: REDUCED (for similar pressure)
Slot effect for higher sec.
air absorption efficiency
Axial tip: OPEN (minimum section)
Air flowrate: INCREASED
Momentum: INCREASED (for similar pressure)
Slot effect for higher sec.
air absorption efficiency
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Peers Conference 2019 – Rotary Kiln Burner
Fives Pillard Rotaflam® Burner – Adjustable momentum principle
Stroke: + 35 mm
Axial tip
CLOSED
Stroke: + 35 mm
Radial tip
CLOSED
Axial tip
OPEN
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Pellet
Secondary circuit
Primary atomizer
Secondary atomizer
Primary circuit
 Fuel
 Liquid fuel injection
Edição:0
Firing
Objective:
Mix the fuel with primary air;
 Achieve the atomization adequate for the fuel;
 EXAMPLE I: mechanical atomization (diagram MY)
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Edição:01 Firing 194
 Ignition moment impact in the flame
(Rotaflam Burner, Coal with medium volatile material)
02 Jan 2006
High Swirl, low axial moment Low swirl, high axial moment
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Images ECRA
Is = 9
Swirl = 0.15
Strong and
narrow flame
Images Lafarge
Edição:0
Firing
Is = 6
Swirl = 0.15
Normal
Flame
Is = 3
Swirl = 0.15
Lazy
Flame
Is = 6
Swirl = 0.25
Strong and
large flame
Is = 6
Swirl = 0.15
Normal
Flame
Is = 6
Swirl = 0.05
Long and
narrow flame
Effect of the moment and of the swirl in the
shape of the flame
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 Alignment of the burner in the kiln
Edição:0
Firing
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The burner should always be aligned with the kiln axel.
If it is in the horizontal, as the kiln axle is at
approximately 3º, the flame touches the materials,
creating local reduction conditions, thus causing the
increase of alkalis and sulphur volatilisation.
 Fuel characteristics
As mentioned in the beginning of the chapter, the characteristics
and the fuel preparation level limit the shape and length of the
flame.
Volatile content (MV):
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Ignition time and distance
MV =>
Fineness :
Fineness => Ignition time and distance
Ash content:
Ashes => Ignition time and distance
Ashes absorb heat
Edição:0
Firing
Mixing different fuels, as for example natural gas with fuel or
coal, makes alterations in the flame length. Besides, it changes
the maximum temperature position as well as the heat transfer
by radiation (different emissions):
Edição:0
Firing
 The flame length is superior to when only one fuel is burnt.
(The necessary air mixes itself more quickly with a fuel, thus
reducing combustion time).
 Changing fuel or burning a fuel mixture demands an adequation
of the burner parameters, in order to avoid flame alterations.
F
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 Fuel mixture effect
70% Coal
30% Pulverised WTC Mud
Edição:0
Firing
100 % Coal
 Fuel mixture effect
(Rotaflam Burner, high swirl / medium axial moment)
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 Flame adjustments
Follow the supplier’s instructions;
Adjust parameters only when the kiln is stable;
Edição:0
Firing
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Make progressive adjustments of one parameter at a time (eg:
axial air or swirl air) and monitor combustion indexes;
Attention:
1) The kiln takes long to react, so time should be given
between alterations to verify exactly what the consequences
are;
2) Axial air is also used to cool the pipe, so it should never be
regulated below a certain level.
COMBUSTION OF
PETCOKE
2011
39
DESIGN OF
FLEXIFLAME
PETCOKE
Combustion of petcoke:
Petcoke is harder to ignite as conventional coal (low volatile)
Petcoke provides a higher flame radiation then coal
Petcoke has a typicall high sulfur content
Petcoke develops a higher NOx formation
Usually petcoke changes the kiln profile
Petcoke needs a special burner design
2011
40
PETCOKE
COMBUSTION
The combustion of petcoke requires:
Quick mixing of secondary air to the flame, to allow the complete
combustion which is iniciated by primary air.
Primary air jets need to accellerate the secondary air.
Internal recirculations are controlling the ignition distance of the fuel
2011
41
Peers Conference 2019 – Rotary Kiln Burner
Atomizing steam pressure
Atomization quality vs. Flame intensity (Lime Reburning Kiln)
NOx (mg/Nm3 at 7%O2)
Lower atomizing steam pressure means bigger droplets, longer and
less intense flame (lower peak temperature, lower NOx)
Fives Pillard Rotaflam® Burner – Liquid Fuel Injectors
 The key parameter for a proper liquid fuel combustion is the
atomization quality.
 The size of the fuel droplets will determine how fast it will burn
and how far it will go. Thus, it is possible to change the flame
length and shape by changing the atomization quality.
Assisted Atomization (steam or compressd air)
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Additional Information
Burner Impulsion
58
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
Thermal Power
59
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
Burner Adjustments
61
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
Steps to Upgrade an Existing Burner
64
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
First Level of Improvement
Increase of burner impulse without burner modification
 Step 1: Check possibility for primary air volume flow /
pressure increase with present equipment


Open throttle valves in primary air ducts
Change burner tip adjustments ->
open burner tip cross sections
Remove any restrictions in primary air duct -> i.e. bends,
sound absorbers
Exclude primary air fan motor restrictions ->
install bigger motor
Change the gear ratio of the primary air fan drive



Steps to Upgrade an Existing Burner
65
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
First Level of Improvement
Increase of burner impulse without burner modification
 Step 2: Upgrade the existing primary air fan



Increase fan speed by use of VSD for primary air fan
Install modified fan wheel
Install volume flow and pressure measurement for CCR
 Step 3: Install bigger primary air fan or an additional fan




Consider the equipment curve of the burner tip, dp = f(V)
Consider the pressure loss by burner jacket tubes
Burner tip curve gives the ratio impulsion/primary air amount
Consultation of burner supplier to take into account
Steps to Upgrade an Existing Burner
66
© 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
Second Level of Improvement
Increase of burner impulse including burner tip or
jacket tube modification
 Step 4: Install modified burner tip
 Optimization of impulse according to primary air fan
 Adaptation of fuel exit velocity, fuel type change
 Change of swirl angle
 New burner tip design, improvement of flame shape
 Step 5: Install modified jacket tube(s)



Reduction of pressure loss
Replacement required, wear rate
AFR utilization

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burner.pptx it take about burner optimization

  • 2.  COMBUSTION REACTION Combustion is a reaction between oxygen and fuel. This oxidation is an exothermic reaction. Correct proportion OXYGEN FUEL FLAME Ignition C O M B U S T I O N R E A C T I O N S Edição:0 Firing 2
  • 3.  BURNERS OBJECTIVE: Insert fuel in the burning zone. Its efficiency depends on the speed it enters in contact with oxygen. They should be planned and regulated by way of setting the heat in the ideal place, by way of not causing damages to the wall (refractory) and to produce as less pollutants and possible (CO, NOx, SO2). B U R N E R S Edição:0 Firing
  • 4. Rotary Kiln Burner & Flame Theory  Function of a rotary kiln burner: • Mix fuel and combustion air to produce a stable flame and to release heat in a way adapted to process requirements.  Diffusion flames: • Burner fed with 100% of the kiln fuels but only ~10% of required combustion air (Primary Air). The other 90% of combustion air comes from the cooler (Secondary Air), to recover the material energy. Thus, with only 10% of the combustion air, the burner must be able to produce:  An adjustable thermal profile  A stable flame:  Efficient combustion & Reduced air emissions  Impulse (Momentum): • Force generated by the primary air and fuels discharge velocity at the burner tip.  Impulse (N) = Mass flow (kg/s) x Velocity (m/s) • It generates the secondary air and the fuels mixing. • Proportional to the heat release: Specific Impulse (N/MW) C o m bu sti on Peers Conference 2019 – Rotary Kiln Burner
  • 5.  Single stage burners Unique duct to: Fuel + primary air Usually used for short kiln. They can be used for fuel simultaneously with other fuels, and in this case they have to be equipped with an extra pipe in the centre of the duct. B U R N E R S Coal and/or pet cock Edição:0 Firing
  • 6.  Multi-stage burners For a more efficient adjustment in the flame, through primary air, multi-stage burners are used, which are divided in two components, axial and radial, with the fuel being introduced also through a tube which is concentric with others. They can be used for only one fuel or for several alternately or simultaneously (gas, liquid or solid). B U R N E R S axial transport swirl Edição:0 Firing
  • 7. B U R N E R S Edição:0 Firing Axial air is injected towards the kiln axel. The swirl air is injected towards the kiln burner (the angle is one of the burner’s project parameters) .  Multi-stage burners The swirl component of radial air creates a rotating air flow around the kiln (like a screw), which also pushes in towards the exterior. As the swirl air is located internally to the axial air, its increase causes flame enlargement.
  • 8.  Pillard Rotaflam  FLS Duoflex  Unitherm M.A.S.  Greco-Enfil / Flexiflame (new)  KHD Pyrojet / Pyrostream  Polysius Polflame Burner Suppliers Overview Most used burners in Holcim plants 42 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 9. MAIN BURNER Lafarge KHD MAS Unitherm Greco Pillard Rotaflam C O M B U S T I O N S Y S T E M S Edição:0 Firing
  • 10. FLS Duoflex Burner – logical PA adjustments  The sum of the axial and swirl air exit cross can be adjusted  Only one fan for axial and swirl channel is used  Burner momentum remains by changing axial/radial split 44 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 11. PYRO-JET Burner ® Central air duct Rotation air Mud duct Per cock duct Axial air oil / solvents / water duct B U R N E R S Edição:0 Firing
  • 12. Fuel Secondary air Axial Air Swirl air B U R N E R S PYRO-JET Burner ® Edição:0 Firing
  • 13. + + Secondary air Secondary air Axial Axial Radial/Swirl Radial/Swirl Central 18 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008 Primary air split up into Axial, Radial and Central Air
  • 14. Primary air and multichannel burner tip Axial air Radial air Nat. gas Pulv. coal Liquid & Solid wastes Axial air Nat. gas Radial air Pulv. coal Liquid & Solid wastes Coal Natural gas Cooling air Radial Air Axial air Radial Air Axial air Coal Natural gas Cooling air 19 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 15. Pillard Rotaflam Burner – highest flexibility  The cross sections of the axial, radial and coal channel can be individually adjusted  Good experience with the updated tip design RV2  New “blowing device” for AFR channel 43 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 16.  Primary air ratio 13 – 15%  Based on stoichiometric combustion air (Amin), excluding transport air Primary air fan pressure > 300 mbar Main Burner Design Criteria  Specific burner Impulsion (momentum) installed for new multi-channel burners: G = 11 N/MW   Solid fuel injection velocities: 35…40 m/s ~30 m/s ~25 m/s 30…45 m/s     Lignite Coal Petcoke AFR 26 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 17. [N/MW] %PA = percentage of primary air [%] Primary air velocity (Bernoulli) : ptip  pressure at burner inlet -5% [m/s] [Pa] tip = air density at burner tip [kg/m3] (T = 50°C, p = ambient pressure) Example: Amount of primary air: PA = 14%; pBurner Inlet = 300 mbar  vPA = 233 m/s  G = 10.9 N/MW Main Burner Design Criteria - Impulsion G  %PAvPA 300 Quick calculation of specific burner impulsion: tip 28 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008 PA v   2 ptip
  • 18.  Primary air ratio 13 – 15% Main Burner Design Criteria  Specific burner Impulsion (momentum) installed for new multi-channel burners: G = 11 N/MW   Based on stoichiometric combustion air (Amin), excluding transport air Primary air fan pressure > 300 mbar  Solid fuel injection velocities: 35…40 m/s ~30 m/s ~25 m/s 30…45 m/s     Lignite Coal Petcoke AFR 30 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 19. Unitherm M.A.S. Burner – all adjustable swirl air  Brings the whole primary air amount into swirl  Single air jet penetration with several nozzles  Continuous swirl adjustment between 0 - 40° 45 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 21. Edição:01 Firing 170 Swirl Air Axial Air Pet coke ASB Animal Meal Used oils Central Ar B U R N E R S 02 Jan 2006  LAFARGE BURNER
  • 22. Independent ring jets, with nebulization per auxiliary fluid (compressed air or vapour); open chamber type nozzle. Burner with three adjustment air ducts. Each ring for solid fuel and central duct for the alternative solid fuel. B U R N E R S GRECO Burner Edição:0 Firing
  • 23. DESIGN OF FLEXIFLAME BURNERS FOR PETCOKE 2011 23 EXTERNAL AIR TANGENTIAL AIR (ROTATION) COAL/PETCOKE DISPERSION AIR (ROTATION) CENTRAL AIR (RECIRCULATION/COOLING SLUDGES / ANIMALMEAL IGNITOR MIXING AIR FOR ASF RDF / FLUFF DOUBLE SWIRL EFFECT
  • 26. Peers Conference 2019 – Rotary Kiln Burner Fives Pillard Rotaflam® Burner – Multichannel Burner  Adjustable tips cross section during operation  Independently adjustable primary air & natural gas pressure & flowrates 2. Central stabilizer  Improved flame stability (bluff body = internal recirculation)  Possibility for integrated warm-up burner for gaseous or liquid fuel  Possibility for integrated igniter & flame detection  Possibility for integrated lance for solid, liquid or gaseous fuels 3. Fuel concentration for NOx reduction  Fuel injection inside primary air  Low O2 content at flame core  Rotaflam® Multichannel Burner 1. Adjustable Axial air, Radial air & Natural Gas tips  Flame shaping: HFO / NG / Biogas / NCG / Petcoke HFO / Methanol – Ignitor trial C o m bu sti on
  • 27. Peers Conference 2019 – Rotary Kiln Burner Fives Pillard Rotaflam® Burner – Main Characteristics  Coal / Petcoke / Anthracite / Lignite  Central stabilizer • ASF / ALF / HFO / DO • Ignitor / Flame detection C o m bu sti on Axial primary air Adjustable cross section  Radial primary air Adjustable cross section  Natural gas Adjustable cross section
  • 28. Peers Conference 2019 – Rotary Kiln Burner Fives Pillard Rotaflam® Burner – Main Characteristics Axial & Radial air pressure control Axial air tip adjustment Radial air tip adjustment Natural gas Coal Cooling air Axial air Radial air C o m bu sti on
  • 29. Peers Conference 2019 – Rotary Kiln Burner Fives Pillard Rotaflam® Burner – Adjustable momentum principle Axial tip: CLOSED (minimum section) Air flowrate: REDUCED Momentum: REDUCED (for similar pressure) Slot effect for higher sec. air absorption efficiency Axial tip: OPEN (minimum section) Air flowrate: INCREASED Momentum: INCREASED (for similar pressure) Slot effect for higher sec. air absorption efficiency C o m bu sti on
  • 30. Peers Conference 2019 – Rotary Kiln Burner Fives Pillard Rotaflam® Burner – Adjustable momentum principle Stroke: + 35 mm Axial tip CLOSED Stroke: + 35 mm Radial tip CLOSED Axial tip OPEN C o m bu sti on
  • 31. Pellet Secondary circuit Primary atomizer Secondary atomizer Primary circuit  Fuel  Liquid fuel injection Edição:0 Firing Objective: Mix the fuel with primary air;  Achieve the atomization adequate for the fuel;  EXAMPLE I: mechanical atomization (diagram MY) B U R N E R S
  • 32. Edição:01 Firing 194  Ignition moment impact in the flame (Rotaflam Burner, Coal with medium volatile material) 02 Jan 2006 High Swirl, low axial moment Low swirl, high axial moment F L A M E S Images ECRA
  • 33. Is = 9 Swirl = 0.15 Strong and narrow flame Images Lafarge Edição:0 Firing Is = 6 Swirl = 0.15 Normal Flame Is = 3 Swirl = 0.15 Lazy Flame Is = 6 Swirl = 0.25 Strong and large flame Is = 6 Swirl = 0.15 Normal Flame Is = 6 Swirl = 0.05 Long and narrow flame Effect of the moment and of the swirl in the shape of the flame F L A M E S
  • 34.  Alignment of the burner in the kiln Edição:0 Firing F L A M E S The burner should always be aligned with the kiln axel. If it is in the horizontal, as the kiln axle is at approximately 3º, the flame touches the materials, creating local reduction conditions, thus causing the increase of alkalis and sulphur volatilisation.
  • 35.  Fuel characteristics As mentioned in the beginning of the chapter, the characteristics and the fuel preparation level limit the shape and length of the flame. Volatile content (MV): F L A M E S Ignition time and distance MV => Fineness : Fineness => Ignition time and distance Ash content: Ashes => Ignition time and distance Ashes absorb heat Edição:0 Firing
  • 36. Mixing different fuels, as for example natural gas with fuel or coal, makes alterations in the flame length. Besides, it changes the maximum temperature position as well as the heat transfer by radiation (different emissions): Edição:0 Firing  The flame length is superior to when only one fuel is burnt. (The necessary air mixes itself more quickly with a fuel, thus reducing combustion time).  Changing fuel or burning a fuel mixture demands an adequation of the burner parameters, in order to avoid flame alterations. F L A M E S  Fuel mixture effect
  • 37. 70% Coal 30% Pulverised WTC Mud Edição:0 Firing 100 % Coal  Fuel mixture effect (Rotaflam Burner, high swirl / medium axial moment) F L A M E S
  • 38.  Flame adjustments Follow the supplier’s instructions; Adjust parameters only when the kiln is stable; Edição:0 Firing F L A M E S Make progressive adjustments of one parameter at a time (eg: axial air or swirl air) and monitor combustion indexes; Attention: 1) The kiln takes long to react, so time should be given between alterations to verify exactly what the consequences are; 2) Axial air is also used to cool the pipe, so it should never be regulated below a certain level.
  • 40. DESIGN OF FLEXIFLAME PETCOKE Combustion of petcoke: Petcoke is harder to ignite as conventional coal (low volatile) Petcoke provides a higher flame radiation then coal Petcoke has a typicall high sulfur content Petcoke develops a higher NOx formation Usually petcoke changes the kiln profile Petcoke needs a special burner design 2011 40
  • 41. PETCOKE COMBUSTION The combustion of petcoke requires: Quick mixing of secondary air to the flame, to allow the complete combustion which is iniciated by primary air. Primary air jets need to accellerate the secondary air. Internal recirculations are controlling the ignition distance of the fuel 2011 41
  • 42. Peers Conference 2019 – Rotary Kiln Burner Atomizing steam pressure Atomization quality vs. Flame intensity (Lime Reburning Kiln) NOx (mg/Nm3 at 7%O2) Lower atomizing steam pressure means bigger droplets, longer and less intense flame (lower peak temperature, lower NOx) Fives Pillard Rotaflam® Burner – Liquid Fuel Injectors  The key parameter for a proper liquid fuel combustion is the atomization quality.  The size of the fuel droplets will determine how fast it will burn and how far it will go. Thus, it is possible to change the flame length and shape by changing the atomization quality. Assisted Atomization (steam or compressd air) C o m bu sti on
  • 44. Burner Impulsion 58 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 45. Thermal Power 59 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 46. Burner Adjustments 61 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008
  • 47. Steps to Upgrade an Existing Burner 64 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008 First Level of Improvement Increase of burner impulse without burner modification  Step 1: Check possibility for primary air volume flow / pressure increase with present equipment   Open throttle valves in primary air ducts Change burner tip adjustments -> open burner tip cross sections Remove any restrictions in primary air duct -> i.e. bends, sound absorbers Exclude primary air fan motor restrictions -> install bigger motor Change the gear ratio of the primary air fan drive   
  • 48. Steps to Upgrade an Existing Burner 65 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008 First Level of Improvement Increase of burner impulse without burner modification  Step 2: Upgrade the existing primary air fan    Increase fan speed by use of VSD for primary air fan Install modified fan wheel Install volume flow and pressure measurement for CCR  Step 3: Install bigger primary air fan or an additional fan     Consider the equipment curve of the burner tip, dp = f(V) Consider the pressure loss by burner jacket tubes Burner tip curve gives the ratio impulsion/primary air amount Consultation of burner supplier to take into account
  • 49. Steps to Upgrade an Existing Burner 66 © 2008 Holcim/Switzerland Burner – Standard Requirements 12.9.2008 Second Level of Improvement Increase of burner impulse including burner tip or jacket tube modification  Step 4: Install modified burner tip  Optimization of impulse according to primary air fan  Adaptation of fuel exit velocity, fuel type change  Change of swirl angle  New burner tip design, improvement of flame shape  Step 5: Install modified jacket tube(s)    Reduction of pressure loss Replacement required, wear rate AFR utilization