boundary layer effects on the critical nozzle of …
TRANSCRIPT
BOUNDARY LAYER EFFECTS ON THE
CRITICAL NOZZLE OF HYDROGEN SONIC
JET
Marius Paraschivoiu
Farbod Vakilimoghaddam
Mohammadamin Afroosheh
Concordia University
The 6th International Conference on Hydrogen Safety (ICHS)
Yokohama (Japan)
October 19-21, 2015
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Research Goal
Study the Mach number at the nozzle exit of
the under-expanded jet
Objectives
Study the viscous effects which create a fluid throat
which acts as a converging-diverging nozzle;
Study the initial transient effect on the Mach number
inside the exit throat;
Quantify the effect on the mass flow and velocity of the
under-expanded jet.
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Previous Work
Kubo, K., Miyazato, Y., and Matsuo, K., Study
of choked flows through a convergent Nozzle,
Journal of Thermal Science, 19, no. 3, 2010,
pp. 193-197.
Experimental work, Low Reynolds number, Steady
flow; “the main flow Mach number at the nozzle exit is supersonic
when the back pressure ratio is equivalent to the choking
condition, and the Mach number increases as the boundary
layer thickness increases.”
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Navier-Stokes Equations with Large Eddy Simulation model for turbulence
Model| Objectives | Boundary layer effect|
Transport (Advection) Equation: 𝝏𝒄
𝝏𝒕+𝝏(𝒄(𝒖 − 𝒘𝒙))
𝝏𝒙+𝝏(𝒄(𝒗 − 𝒘𝒚))
𝝏𝒚+𝝏(𝒄(𝒘 − 𝒘𝒛))
𝝏𝒛= 𝟎
Abel Nobel Real Gas Law: 𝒑 = (𝟏 − 𝒃𝝆)−𝟏𝝆𝑹𝒎𝒊𝒙𝑻, 𝒃 = 𝟎. 𝟎𝟎𝟕𝟕𝟓 𝒎𝟑 𝒌𝒈
• 𝑐=0 a cell full of hydrogen
• 0<𝑐<1 discontinuity (hydrogen-air interface)
• 𝑐=1 a cell full of air
Spatial Discretization (Convection Flux)
𝟐𝒏𝒅 order Roe-MUSCL scheme
Temporal Discretization
𝟏𝒔𝒕 order Implicit Scheme
Linear Solver
Iterative Method : GMRES
Axisymmetric model| Transient results | Conclusion
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Computational
Domain
3D unstructured
tetrahedral mesh
2D slices of the mesh
small cylindrical orifice
diameter D=1 mm and a
length L=2 mm
14.8 million grid points
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Mach number in the Nozzle
Viscous Mach number distribution
inside the release pipe after 15
micro-second of release for
1) 10 MPa and 2)70 MPa
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
Radial Mach number distribution
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Near Jet Region
Centerline values of
hydrogen jet release
from 1mm orifice after
15 microsecond of
release for A) Mach
number, B) density, C)
pressure, and D)
temperature
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Euler Simulation
Inviscid Mach number distribution inside
the release pipe after 15 micro-second of
release
Mach Distribution
Inviscid 10MPa Inviscid 70MPa
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Geometry : 3D CAD Model
Full 3D CAD Model
Axisymmetric Model : 10 Degree
modelling
Circular orifice diameter : 0.5 mm Hydrogen High Pressure
Chamber
Air Chamber
Hydrogen High Pressure
Chamber
Air Chamber
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Computational Domain
Mesh Statistic
Viscous Case Euler Case
Number of Elements
2,715,484 2,490,247
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Boundary Layer Mesh
AR=1
Boundary Layer Meshing Characteristics
First Layer Height (mm) 2.E-05
y+ 0.7 Aspect Ratio 1.1
Number of Layers 40
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Inviscid simulation based on Euler Equations.
Viscous simulation based on Reynolds Averaged Navier-Stokes (RANS)
Equations.
One transport equation for concentration.
Turbulence Model:
K–omega (k–ω) –SST
Two transport equations (PDE) for :
Turbulence Kinetic Energy (k)
Specific Rate of Dissipation (ω)
Redlich Kwong Real Gas Law:
𝒑 = (𝟏
𝝆− 𝒃 + 𝒄)−𝟏𝑹𝒎𝒊𝒙𝑻 −
𝒂 𝑻
𝟏𝝆
𝟏𝝆 + 𝒃
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
Solution Characteristic
Discretization
Order Second Order
CFL Adaptive time
stepping method
Convergence
criteria 1.0 E-05
Initial
Timestep 5.0 E-09
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Initial and Boundary Conditions
Initial Reservoir Pressure 70MPa &
10MPa
Initial Temperature 300 K
Air mixture fraction 1
Hydrogen mixture fraction 0
Hydrogen & air isentropic exponent (γ) 1.4
Molecular mass of hydrogen (𝑴𝑯𝟐) 2.016 g/mol
Molecular mass of air (𝑴𝒂𝒊𝒓) 28.96 g/mol
Convergence Criteria 𝟏𝟎−𝟓
Time step adaptive
The effect of the gravity on the fluid is neglected.
No-slip and adiabatic solid walls.
Non-reflecting farfield boundary conditions.
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Flow at after 15 micro seconds
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Transient Flow Simulation
0.9
0.95
1
1.05
1.1
1.15
1.2
1.25
1.3
-0.002 -0.0015 -0.001 -0.0005 0
Mach Number
5µs 10µs 15µs 20µs 30µs
3.00E+06
3.50E+06
4.00E+06
4.50E+06
5.00E+06
5.50E+06
6.00E+06
-0.002 -0.0015 -0.001 -0.0005 0
Pressure
5 µs 10 µs 15 µs 20 µs 30 µs
Euler Case Study
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Transient Flow Simulation
1
1.01
1.02
1.03
1.04
1.05
1.06
-0.002 -0.0015 -0.001 -0.0005 0
Mach Number
100 µs 200 µs 300 µs
4.80E+06
4.85E+06
4.90E+06
4.95E+06
5.00E+06
5.05E+06
5.10E+06
5.15E+06
5.20E+06
-0.002 -0.0015 -0.001 -0.0005 0
Pressure
100 µs 200 µs 300 µs
Euler Case Study
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Transient Flow Simulation
0.85
0.9
0.95
1
1.05
1.1
1.15
1.2
1.25
1.3
-0 .002 -0 .0015 -0 .001 -0 .0005 0
MACH NUMBER
5 µs 10 µs 15 µs 25 µs
Viscous-SST Case Study
3.00E+06
3.50E+06
4.00E+06
4.50E+06
5.00E+06
5.50E+06
6.00E+06
6.50E+06
-0 .002 -0 .0015 -0 .001 -0 .0005 0
PRESSURE
5 µs 10 µs 15 µs 25 µs
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Transient Flow Simulation
Euler-Viscous Case Comparison ( t =15µs)
0.9
0.95
1
1.05
1.1
1.15
-0 .002 -0 .0015 -0 .001 -0 .0005 0
MACH-NUMBER
VISCOUS-SST-15 µs EULER-15 µs
4.50E+06
4.70E+06
4.90E+06
5.10E+06
5.30E+06
5.50E+06
5.70E+06
5.90E+06
6.10E+06
-0 .002 -0 .0015 -0 .001 -0 .0005 0
PRESSURE
VISCOUS-SST-15µs EULER-15µs
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Conclusion
Boundary layer in the nozzle leads to lower mass flow
rate;
Boundary layer is difficult to capture accurately;
Importance of transient effect in the first 100
micro-seconds;
Euler solution provides a worse case scenario compared
with a Navier-Stokes solution.
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion
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Transient Flow Simulation
Converging Diverging Boundary Layer
Model| Objectives | Boundary layer effect| Axisymmetric model| Transient results | Conclusion