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An experimental and numerical investigation of heat transfer downstream of a normal film cooling injection slot Sun, Yuping
Abstract
This thesis presents an experimental and numerical investigation of turbulent heat transfer associated with film cooling from a 2D slot. To determine the film cooling heat transfer coefficient, detailed mass transfer measurements have been carried out downstream of a normal film cooling injection slot. The plate downstream of the injection location is porous and air contaminated with propane or methane is bled through the plate beneath it. By measuring the propane or methane concentration very close to the wall, mass transfer measurements are conducted for film cooling mass flow ratios ranging from zero to 0.5. The mass transfer coefficients are calculated using a wall function correction formula, which corrects the measurements for displacement from the surface, and are then related directly to corresponding heat transfer coefficients using the mass/heat transfer analogy. The validity of the method and the wall function correction formula are checked by examining the case with zero film coolant injection, a situation analogous to the well-known turbulent boundary layer mass/heat transfer with impermeable/unheated starting length. Good agreement with data in the literature is obtained for this experiment. For film cooling with low mass flow ratios (M 0.1), heat transfer coefficients close to those of a conventional turbulent boundary layer are obtained. At high values of mass flow ratio (M > 0.1) heat transfer coefficients similar to those of turbulent separated flows are observed, reflecting the important effect of the separation bubble just downstream of injection. Numerical calculations of turbulent flow and heat transfer associated with film cooling have been carried out to validate the present mass transfer method and to ensure that the heat transfer coefficients obtained using the mass/heat transfer analogy are valid. In the present study, the time-averaged continuity equation, Navier Stokes equations and thermal energy equation, together with the k-ε a turbulence model, are used to describe the turbulent flow and heat transfer. This system of governing equations is discretized using the control volume method. To obtain the numerical solution of the resulting finite difference equations, a novel multi-grid method with no boundary correction is proposed. This method differs from the FAS multi-grid method in that it employs a special multi-grid procedure to ensure that the correction on the coarse grids vanishes along the boundary, and it offers an easier procedure to overcome difficulties arising from the boundary treatment in both discretization and the multi-grid algorithm. The performance of the method is examined using the laminar cavity flow and the turbulent boundary layer flow, which indicates that it is efficient and can overcome difficulties resulting from the near-wall treatment and the discrete vorticity boundary condition. Numerical simulation of turbulent flow and heat transfer associated with film cooling are conducted using the proposed multigrid method. Detailed turbulent flow field and heat transfer results are obtained for film cooling mass flow ratios ranging from zero to 0.5. The numerical results show that the standard k-ε a turbulence model, together with the standard wall function, underpredicts considerably the heat transfer coefficients of film cooling at high mass flow ratio, and therefore, is not appropriate for accurate prediction of turbulent heat transfer in the region of flow separation. However, with a modified near-wall treatment, predictions of heat transfer coefficients compare well with the experimental results obtained using the mass/heat transfer analogy. Numerical calculations also show that the overall effect of the wall transpiration for the blowing rates used for the mass transfer measurements on heat transfer is negligible. The present study finally concludes that both the numerical and mass transfer method can be used to investigate film cooling heat transfer with fair accuracy.
Item Metadata
Title |
An experimental and numerical investigation of heat transfer downstream of a normal film cooling injection slot
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Creator | |
Publisher |
University of British Columbia
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Date Issued |
1995
|
Description |
This thesis presents an experimental and numerical investigation of turbulent heat transfer
associated with film cooling from a 2D slot. To determine the film cooling heat transfer
coefficient, detailed mass transfer measurements have been carried out downstream of a
normal film cooling injection slot. The plate downstream of the injection location is porous
and air contaminated with propane or methane is bled through the plate beneath it. By
measuring the propane or methane concentration very close to the wall, mass transfer
measurements are conducted for film cooling mass flow ratios ranging from zero to 0.5. The
mass transfer coefficients are calculated using a wall function correction formula, which
corrects the measurements for displacement from the surface, and are then related directly to
corresponding heat transfer coefficients using the mass/heat transfer analogy. The validity of
the method and the wall function correction formula are checked by examining the case with
zero film coolant injection, a situation analogous to the well-known turbulent boundary layer
mass/heat transfer with impermeable/unheated starting length. Good agreement with data in
the literature is obtained for this experiment. For film cooling with low mass flow ratios
(M 0.1), heat transfer coefficients close to those of a conventional turbulent boundary layer
are obtained. At high values of mass flow ratio (M > 0.1) heat transfer coefficients similar to
those of turbulent separated flows are observed, reflecting the important effect of the
separation bubble just downstream of injection. Numerical calculations of turbulent flow and
heat transfer associated with film cooling have been carried out to validate the present mass
transfer method and to ensure that the heat transfer coefficients obtained using the mass/heat
transfer analogy are valid. In the present study, the time-averaged continuity equation, Navier
Stokes equations and thermal energy equation, together with the k-ε
a turbulence model, are
used to describe the turbulent flow and heat transfer. This system of governing equations is
discretized using the control volume method. To obtain the numerical solution of the resulting
finite difference equations, a novel multi-grid method with no boundary correction is
proposed. This method differs from the FAS multi-grid method in that it employs a special
multi-grid procedure to ensure that the correction on the coarse grids vanishes along the
boundary, and it offers an easier procedure to overcome difficulties arising from the boundary
treatment in both discretization and the multi-grid algorithm. The performance of the method
is examined using the laminar cavity flow and the turbulent boundary layer flow, which
indicates that it is efficient and can overcome difficulties resulting from the near-wall
treatment and the discrete vorticity boundary condition. Numerical simulation of turbulent
flow and heat transfer associated with film cooling are conducted using the proposed multigrid
method. Detailed turbulent flow field and heat transfer results are obtained for film
cooling mass flow ratios ranging from zero to 0.5. The numerical results show that the
standard k-ε a turbulence model, together with the standard wall function, underpredicts
considerably the heat transfer coefficients of film cooling at high mass flow ratio, and
therefore, is not appropriate for accurate prediction of turbulent heat transfer in the region of
flow separation. However, with a modified near-wall treatment, predictions of heat transfer
coefficients compare well with the experimental results obtained using the mass/heat transfer
analogy. Numerical calculations also show that the overall effect of the wall transpiration for
the blowing rates used for the mass transfer measurements on heat transfer is negligible. The
present study finally concludes that both the numerical and mass transfer method can be used
to investigate film cooling heat transfer with fair accuracy.
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Extent |
3656008 bytes
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Genre | |
Type | |
File Format |
application/pdf
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Language |
eng
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Date Available |
2009-06-11
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Provider |
Vancouver : University of British Columbia Library
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Rights |
For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use.
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DOI |
10.14288/1.0088918
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URI | |
Degree | |
Program | |
Affiliation | |
Degree Grantor |
University of British Columbia
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Graduation Date |
1995-05
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Campus | |
Scholarly Level |
Graduate
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Aggregated Source Repository |
DSpace
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Item Media
Item Citations and Data
Rights
For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use.