1
Institut für Verbrennungstechnik - Institute of Combustion TechnologyD. Panara, R. Dannecker, B.Noll
Institut für Verbrennungstechnik
DLR Deutsches Zentrum für Luft- und Raumfahrt e.V.
Mitglied der Herrmann von Helmholtz-Gemeinschaft Deutscher Forschungszentren HGF
Stuttgart
FLUISTCOM
Fluid Structure
Interaction for Combustion Systems
( MRTN-CT-2003-504183)
Combustion Instability Effects and
Aero-Thermal Near-Wall Response
Agenda 12-Months Progress Meeting
2
Institut für Verbrennungstechnik - Institute of Combustion Technology•
January
2003
-
University of Florence
,
Mechanical Engineering
Diploma
• Thesis title: Finflo and Tascflow a comparison between two different
Navier-Stokes CFD codes in strong curvature applications
•
Supervisors:
Prof. T.
Siikonen
( Helsinki University of Tech.)
Prof. F.
Martelli
and P.
Adami
( University of Florence )
•
Jan-April
2003
-
Helsinki University of Technology
,
Researcher
• Thesis Publication, Helsinki University Laboratory Report.
•
June-July
2003
-
Teknomeccanica s.r.l.
, Italy,
Control and Assembling
•
July-Sept
2003
-
Nuovo Pignone GE oil & Gas
, Italy,
Quality Engineer
•
Sept 2003-June 2004
-
Von Karman Institute for Fluid Dynamic
Diploma Course, Department of Turbomachinery and Propulsion
• Project title:
Quasi-3D Unsteady Numerical Investigation of Clocking Effects
in 1&1/2 Stage Transonic Turbine
• Supervisor: Prof.
R. Denos
3
Institut für Verbrennungstechnik - Institute of Combustion TechnologyOverview
Literature Research on Pulsating Flow
Experimental Evidences
Thermal Boundary Layer
Viscous Boundary Layer
Numerical Models
4
Institut für Verbrennungstechnik - Institute of Combustion TechnologyNear Wall Aerodynamic Response
in Pulsating Pipe Flows
Viscous Boundary Layer
•
Thermal Boundary Layer
•
Numerical Models
•
ISAAC
Oscillating Flow:
υ
VD
c
=
Re
υ
m
w
aU
=
Re
π
2
T
U
a
m
=
ω
υ
2
=
s
l
s
l
D
R
2
=
δ
Turbulent
800
Re
Laminar
400
Re
≥
≤
s sl
l
υ
s
l
l
U
s0
Re
=
Pulsating Flow:
)
sin(
)
(
t
V
U
t
U
=
+
m
ω
)
sin(
)
(
t
U
t
U
=
m
ω
Source: C.R.Lodahl, et al.: J.Fluid Mech., Vol.373, 1998 Source: A.Scotti, U. Piomelli : Physics of Fluids,13(5), 20015
Institut für Verbrennungstechnik - Institute of Combustion TechnologyTurbulent Flows, Characteristic Parameters
0.05
05
.
0
001
.
0
0.001
≥
≤
≤
≤
+ + +ω
ω
ω
2 τωυ
ω
u
=
+ρ
τ
τ wu
=
)
,
(
)
,
(
~
)
(
)
,
(
x
t
u
x
u
x
t
u
x
t
u
r
r
=
r
r
+
r
r
+
r
′
r
m ucU
V
a
=
Source: M.Gündogdu, M.Carpinlioglu : JSME int. Journal, 42(3), 1999Oscillating Turbulent Flow:
Pulsating Turbulent Flow:
)
sin(
)
(
t
V
U
t
U
=
+
m
ω
)
sin(
)
(
t
U
t
U
=
m
ω
Quasi Steady Flow
Intermediate
Frequency
Quasi-Laminar
=
∫
=
T
w
c
dt
T
0
~
1
τ
τ
τ
τ
Source: C.R.Lodahl, et al.: J.Fluid Mech., Vol.373, 1998•Mean parameters little affected
•Discrepancy close to bursting frequency
•Effects in the Stoke-layers
•Phase shift of _
cup to 45°
•Mean parameters affected
•_/_
cup to 4
•Strong unsteady effects
•Re-laminarization can occur
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Institut für Verbrennungstechnik - Institute of Combustion TechnologyNear Wall Thermal Response
• Lacking of experimental data for current dominated flow
•Contradictory results in both laminar and turbulent
flow conditions about the effect of oscillations on mean
flow quantities
•Measured a phase shift up to 180
º
for the wall heat transfer
•In low-amplitude pulsating flows (source Valueva 2002)
•Frequency range 20 to 1000Hz
• Measured heat transfer increases
•In wave dominated pulsating flows (source Dec, Keller and Arpaci,1992)
• Frequency range ~100Hz
• Measured heat transfer increases up to a factor of 5 over steady flow
• The Reynolds analogy proved not to hold
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Institut für Verbrennungstechnik - Institute of Combustion Technology
Viscous Boundary Layer
•
Thermal Boundary Layer
Numerical Models
•
ISAAC
ε
ν
ε
ε
ε
σ
ν
ν
ε
ε
ε
ε
σ
ν
ν
ε
µ
µ
ε
ε
ε
~
~
~
~
~
~
~
2
2
2
2
1
1
k
f
C
D
E
x
x
k
f
c
k
f
c
x
u
t
x
k
x
x
k
u
t
k
t
i
t
i
i
i
i
k
t
i
i
i
=
+
=
+
∂
∂
+
∂
∂
+
−
=
∂
∂
+
∂
∂
∂
∂
+
∂
∂
+
−
=
∂
∂
+
∂
∂
P
P
2 2 2y
k
D
y
k
w wν
ν
ε
=
∂
∂
=
•Pressure-strain
•Molecular viscosity
Non zero value of
ε
at the wall
j
i
i
i
x
u
u
u
∂
∂
′
′
−
=
P
=
≠
=
j
i
j
i
ij
for
3
for
0
δ
ij ij j i i j j i t j ik
x
u
x
u
x
u
u
u
υ
δ
δ
3
2
~
3
2
~
~
−
∂
∂
−
∂
∂
+
∂
∂
=
′
′
−
•Low-Reynolds model
coefficients
•Correction for non local
isotropy
•
Full Reynolds model
•
Critical closure
Pressure-Strain term
(fluctuating pressure)
•
Two-equation model
•
Inaccurate
formulation
for pulsating flows
•
Accurate formulations
for curvature and
rotation
Turbulence Modeling
Source:
Fan, Lakshminarayana
and Barnett, AIAA J.
Oct. 1993
8
Institut für Verbrennungstechnik - Institute of Combustion TechnologyStrategy of Investigation
Navier-Stokes CFD Code: ISAAC
•
High Turbulence Capabilities
•
K-_ Models
:
•
Low-Reynolds
•SAA : Speziale,Abid,Anderson
•ZSGS : Zhang,So,Gatski,Speziale
•ZSSL : Zhang,So,Speziale,Lai
•
High-Reynolds
•HIGH RE: standard
•RNG : Renormalization Group
•ADRM: Anisotropic Dissipation Rate
•
K-_ Models:
•Low-Reynolds
•K OMEGA: Wilcox
•
Reynolds Stress Model
•
Explicit Algebraic Reynolds Stress Model
Problems
•Code applicability to Incompressible test cases
•Proper extension of B.C. to oscillating flows
Viscous Boundary Layer
•
Thermal Boundary Layer
•
Numerical Models
ISAAC
•
Developed by Morrison, J. H for a NASA contract
Now freely available from www.sourceforge.com
•
Structured
•
Multigrid
•
Unsteady
•
Explicit Runge-Kutta
•
Implicit Pseudo Time Stepping
( up to II order)
•
Implicit:
•AF3F: Diagonalized Spatially Split Approx. Factorization
•
Compressible:
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Institut für Verbrennungstechnik - Institute of Combustion TechnologyConclusions
An overview on experimental evidences on pulsating flow has
been presented
The necessity of a better understanding of the aero-thermal
near-wall flow behavior has been in deep analyzed
An extensive bibliography on test cases and proposed models
for unsteady flows have been acquired.
The ISAAC code has been tested for the future investigations
The limitations of the code have been addressed
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Institut für Verbrennungstechnik - Institute of Combustion Technology11
Institut für Verbrennungstechnik - Institute of Combustion Technology12
Institut für Verbrennungstechnik - Institute of Combustion TechnologyTurbulence Modeling
• Algebraic eddy viscosity models
• Two equations high-Reynolds model + Wall functions
• Two equations low-Reynolds model
• Full Reynolds stress models
• Two equations low Reynolds model +
Unsteady near-wall corrections
Inaccurate: Important role of transport of turbulent quantities
Inaccurate: Steady flow wall function not suited
Inaccurate: Eddy viscosity isotropy assumption
Inaccurate: Insufficient near wall treatment
Viscous Boundary Layer
•
Thermal Boundary Layer
Numerical Models
•
ISAAC
Source:
Fan, Lakshminarayana
and Barnett, AIAA J.
Oct. 1993
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Institut für Verbrennungstechnik - Institute of Combustion Technology14
Institut für Verbrennungstechnik - Institute of Combustion Technology•
Sustainable Energy
•
Combustion Instabilities
•
Near-wall fluid structures
•
Strategy of investigation
References: AERODYNAMICS
•General overview aerodynamics:
•Low amplitude
•Gundogdu and Carpinlioglu,JSME,vol42,n3,1999
•Scotti and Piomelli,physics of fluid,vol13,n5,2001
•Low and High amplitude
•Lodahl and Sumer and Fredsoe, J.Fluid Mech,vol373,1998
•Test case also (pipe water)
•Koehler and Patankar and Ibele,NASA-CR187177
•Test cases
•Cousteix and Houdeville (flat plate air)
•Tardu and Binder and Blackwelder (pipe water)
•Ideas for unsteady turbulence models:
•Fan and Lakshminarayana,AIAA,vol31,1993
•Mankbadi and Liu, J.Fluid Mech,vol238,1992
•Hanjalic and Stosic
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Institut für Verbrennungstechnik - Institute of Combustion Technology•
Sustainable Energy
•
Combustion Instabilities
•
Near-wall fluid structures
•
Strategy of investigation
References: HEAT TRANSFER
•Low amplitude
•Valueva,High Temperature,vol37,n5,1999
•Test case also ( oscillating, compressible incompressible)
•Ideas for unsteady turbulence model
•Ideas for unsteady Energy equation
•High amplitude
•Dec and Keller,Int.J.Heat Mass Transfer,vol35,n9,1992
•Test case also (oscillating combustor tail pipe)
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Institut für Verbrennungstechnik - Institute of Combustion Technology•
Sustainable Energy
•
Combustion Instabilities
•
Near-wall fluid structures
•
Strategy of investigation
•Morrison, J. H., Flux Difference Split Scheme for Turbulent Transport Equations, AIAA Paper 90-5251, October 1990.•Morrison, J. H., A Compressible Navier-Stokes Solver with Two-Equation and Reynolds Stress Turbulence Closure Models, NASA CR-4440, May 1992.
•Morrison, J. H. and Korte, J. J., Implementation of Vigneron's Streamwise Pressure Gradient Approximation in Parabolized Navier-Stokes Equations, AIAA Journal, Vol. 30, No. 12, November 1992.
•Morrison, J. H., Gatski, T. B., Sommer, T. P., Zhang, H. S., and So, R. M. C., Evaluation of a Near-Wall Turbulent Closure Model in Predicting Compressible Ramp Flows, Near-Wall Turbulent Flows, Eds. R. M. C. So, C. G. Speziale, and B. E. Launder, Elsevier Science Publishers B.V., 1993.
•Chenault, C. F., Development and Implementation of a Scramjet Cycle Analysis Code With a Finite-Rate-Chemistry Combustion Model For Use on A Personal Computer, Masters Thesis, Air Force Institute of Technology, December 1993. AFIT/GAE/ENY/93D-7
•Abid, R., Gatski, T. B., and Morrison, J. H., Assessment of Pressure-Strain Models in Predicting Compressible, Turbulent Ramp Flows, AIAA Journal, Vol. 33, No. 1, January 1995.
•Vahala, G., Vahala, L., Morrison, J., Krasheninnikov, S., and Sigmar, D., Effects of Neutral Three-Dimensional Turbulence in the Gas Blanket Regime for Divertors, Physics Letters A, Vol. 205, 1995, pp. 266-273.
•Vahala, G., Vahala, L., Morrison, J., Krasheninnikov, S., and Sigmar, D., Toroidal Wall Heat Flux and Conductivity Profiles Due to Neutral 3D Turbulence in the Gas Blanket Regime for Divertors, Contrib. Plasma Phys., Vol. 36, No. 2/3, 1996, pp. 304-308.
•Gatski, T. B., Prediction of Airfoil Characteristics with Higher Order Turbulence Models, NASA Technical Memorandum 110246, April, 1996. Abstract | PDF | Postscript
•Gatski, T. B., Airfoil Stall Prediction Using a Two-Equation and an Explicit Algebraic Stress Model, Advances in Turbulence VI, Eds. Gavrilakis, S., Machiels, L., and Monkewitz, P. A., Kluwer Academic Publishers, 1996.
•Ristorcelli, J. R. and Morrison, J. H., The Favre-Reynolds Average Distinction and a Consistent Gradient Transport Expression for the Dissipation, Physics of Fluids, Vol. 8, No. 9, September 1996.
•Abid, R., Morrison, J. H., Gatski, T. B., and Speziale, C. G., Prediction of Aerodynamic Flows with a New Explicit Algebraic Stress Model, AIAA Journal, Vol. 34, No. 12, December 1996.