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Characterization of fuel spray for a marine burner back-spill atomizer
Giovanni Cafaggi*
Co-Authors:
Peter Arendt Jensen
Peter Glarborg
Sønnik Clausen
Kim Dam-Johansen
* Corresponding author: [email protected]
DTU Chemical Engineering, Technical University of Denmark
Agenda
30 May 20182
• Introduction to the project
• Spray characterization setup
• Selected results
• Conclusions and future work
DTU Chemical Engineering, Technical University of Denmark 30 May 20183
Background
Project goals:
• Support the development of a new burner:
– Lower NOx emissions
– Multi-fuel capability
• Set up reliable CFD simulations to evaluate further improvements
DTU Chemical Engineering, Technical University of Denmark 30 May 20184
CFD background and contribution
2% CO surface,fuel droplets in black
Temperature
0
10
20
30
40
50
60
70
80
90
100
0
5
10
15
20
25
0 50 100 150 200
Num
ber
of
dro
ple
ts [
%]
Dro
ple
t m
ean d
iam
ete
r [µ
m]
Distance from the nozzle [mm]
Simulated droplet evaporation
Mean diameter
Evaporated Droplets
• Sensitivity to droplet size
and velocity.
• Range for experimental
spray measurements.
DTU Chemical Engineering, Technical University of Denmark
Spray setup commissioning
30 May 20185
• CFD showed that the flame stability is highly dependant from the droplet size and velocity distributions.
• The setup has been built for direct measurements of both using optical imaging methods.
• The setup is able to reproduce the operating conditions of the atomizer in the full scale boiler (matching flows and operating pressures, spill-return nozzle).
DTU Chemical Engineering, Technical University of Denmark
Pump
Tap water
Tank
Pressuregauge 1
Nozzle holder
Nozzle
Spray
Pressuregauge 2
Safety valve
Membrane tank
Flowmeter 1
Flow meter 2Backpressure
valve 2
Backpressure valve 1
Spray setup
30 May 20186
Nozzle section
Setup PID
Working nozzle
DTU Chemical Engineering, Technical University of Denmark
Spray setup – measurement technology
• Led pulser (1μs), ccv camera, stereoscopic lens (2.5 μm resolution)
• Pairs of images to find droplet velocities
• Image analysis with in-house software
7
2.41mm
3.24mm
0.86mm
F. Cernuschi et al. 2017 [4]
30 May 2018
Imaging system
Observed volume
Pair of images 1 µs apart
DTU Chemical Engineering, Technical University of Denmark
Spray setup – measurement technology
8
F. Cernuschi et al. 2017 [4]
2.41mm
3.24mm
0.86mm
• Led pulser (1μs), ccv camera, stereoscopic lens (2.5 μm resolution)
• Pairs of images to find droplet velocities
• Image analysis with in-house software
30 May 2018
Imaging system
Observed volume
Pair of images 1 µs apart
DTU Chemical Engineering, Technical University of Denmark
Spray setup – measurement technology
• Led pulser (1μs), ccv camera, stereoscopic lens (2.5 μm resolution)
• Pairs of images to find droplet velocities
• Image analysis with in-house software
9
2.41mm
3.24mm
0.86mm
F. Cernuschi et al. 2017 [4]
30 May 2018
Imaging system
Observed volume
Pair of images 1 µs apart
DTU Chemical Engineering, Technical University of Denmark
Spray setup – measurement technology
10
F. Cernuschi et al. 2017 [4]
2.41mm
3.24mm
0.86mm
• Led pulser (1μs), ccv camera, stereoscopic lens (2.5 μm resolution)
• Pairs of images to find droplet velocities
• Image analysis with in-house software
30 May 2018
Imaging system
Observed volume
Pair of images 1 µs apart
DTU Chemical Engineering, Technical University of Denmark 30 May 201811
Images Extracted data
Spray setup - PostprocessingNumber based particle size distribution
at 15 mm radial distance
Droplet pairing criteria:
• Area
• Sharpness
• Position
DTU Chemical Engineering, Technical University of Denmark 30 May 201812
Images Extracted data
Droplet pairing and analysis
Spray setup - PostprocessingNumber based particle size distribution
at 15 mm radial distance
DTU Chemical Engineering, Technical University of Denmark
Spray setup - Results
30 May 201813
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
DTU Chemical Engineering, Technical University of Denmark
Spray setup - results
30 May 201814
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
0
5
10
15
20
25
30
0 50 100 150 200
Velo
city m
agnitude [
m/s
]
Distance from injection [mm]
Average droplet velocity from spray setup simulations and experiments
SS distance based
SS volume based
experiments
transient distance based
transient volume based
Preliminary spray setup CFD transient simulation
DTU Chemical Engineering, Technical University of Denmark
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
0
20
40
60
80
100
120
0 10 20 30 40 50 60
SMD
Spray setup - results
30 May 201815
66% load
Experimental results match the simulation regarding the stratification
of droplets according to their size
Simulations
Experimental measurements
33% load
100% load
[μm
]
Angle with spray axis [o]
Droplets diameters
DTU Chemical Engineering, Technical University of Denmark
0.00E+00
5.00E-05
1.00E-04
1.50E-04
2.00E-04
0 10 20 30 40 50 60
Volume fraction
Spray setup - results
16
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
Angle with spray axis [o]
[μm
][#
]
[-]
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Droplet in each image
0
20
40
60
80
100
120
0 10 20 30 40 50 60
SMD
30 May 2018
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Average velocity
[m/s
]
Angle with spray axis [o]
DTU Chemical Engineering, Technical University of Denmark
0.00E+00
5.00E-05
1.00E-04
1.50E-04
2.00E-04
0 10 20 30 40 50 60
Volume fraction
Spray setup - results
17
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
Angle with spray axis [o]
[μm
][#
]
[-]
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Droplet in each image
0
20
40
60
80
100
120
0 10 20 30 40 50 60
SMD
30 May 2018
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Average velocity
[m/s
]
Angle with spray axis [o]
DTU Chemical Engineering, Technical University of Denmark
0.00E+00
5.00E-05
1.00E-04
1.50E-04
2.00E-04
0 10 20 30 40 50 60
Volume fraction
Spray setup - results
18
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
Angle with spray axis [o]
[μm
][#
]
[-]
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Droplet in each image
0
20
40
60
80
100
120
0 10 20 30 40 50 60
SMD
30 May 2018
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Average velocity
[m/s
]
Angle with spray axis [o]
DTU Chemical Engineering, Technical University of Denmark
0.00E+00
5.00E-05
1.00E-04
1.50E-04
2.00E-04
0 10 20 30 40 50 60
Volume fraction
Spray setup - results
19
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
Angle with spray axis [o]
[μm
][#
]
[-]
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Droplet in each image
0
20
40
60
80
100
120
0 10 20 30 40 50 60
SMD
30 May 2018
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Average velocity
[m/s
]
Angle with spray axis [o]
DTU Chemical Engineering, Technical University of Denmark
0.00E+00
5.00E-05
1.00E-04
1.50E-04
2.00E-04
0 10 20 30 40 50 60
Volume fraction
Spray setup - results
20
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
Angle with spray axis [o]
[μm
][#
]
[-]
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Droplet in each image
0
20
40
60
80
100
120
0 10 20 30 40 50 60
SMD
30 May 2018
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Average velocity
[m/s
]
Angle with spray axis [o]
DTU Chemical Engineering, Technical University of Denmark
0.00E+00
5.00E-05
1.00E-04
1.50E-04
2.00E-04
0 10 20 30 40 50 60
Volume fraction
Spray setup - results
21
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
Angle with spray axis [o]
[μm
][#
]
[-]
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Droplet in each image
0
20
40
60
80
100
120
0 10 20 30 40 50 60
SMD
30 May 2018
0
5
10
15
20
25
30
35
0 10 20 30 40 50 60
Average velocity
[m/s
]
Angle with spray axis [o]
DTU Chemical Engineering, Technical University of Denmark
Spray setup - results
30 May 201822
• Experimentally based data:
– Droplet velocity distribution
– Droplet density distribution
– Droplet size distribution
– Droplet volume fraction distribution
– Partial flow behaviour
0
5
10
15
20
25
30
35
0 25 50 75 100 125 150 175
Droplet in each image
0
20
40
60
80
100
120
0 25 50 75 100 125 150 175
SMD
0.00E+00
5.00E-05
1.00E-04
1.50E-04
2.00E-04
0 25 50 75 100 125 150 175
Volume fraction
Angle scaled on highest coverage [%]
[μm
][#
]
[-]
0
5
10
15
20
25
30
35
0 25 50 75 100 125 150 175
Average velocity
Angle scaled on highest coverage [%]
[m/s
]
DTU Chemical Engineering, Technical University of Denmark
Conclusions
• Measurements at different loads showed that it has little effect on particle size,
droplet concentration and volume fraction distribution.
• On the other hand, spray cone angle and velocity are heavily affected by
changes in load.
• Even if the volume fraction is low, there is a large number of droplet in the
hollow part of the cone.
• Data from the spray setup matched expectations and CFD simulations
23 30 May 2018
DTU Chemical Engineering, Technical University of Denmark
Future work
• Further experiments should be carried out to observe spray characteristics at
various axial distances and to check if the CFD results are matched also further
away from the nozzle.
• Spray setup improvements to avoid droplet recirculation and avoid liquid spills
• Water/glycerol solutions with surfactants for the spray setup (viscosity and
surface tension): design of model fluids to evaluate spray characteristics of
different fuels
24 30 May 2018
DTU Chemical Engineering, Technical University of Denmark
Thank you for your attention