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Internal Cooling of a Hot Turbine Structure
Zahra Ghorbani-TariDivision of Heat Transfer, Department of Energy Sciences
Lund University
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Part 1 : Introduction
Part 2 : Calibration of wide-band LCStrategy of calibrationResult
HT measurement in smooth channel flowPreparation of test sectionMethodologyResult
Concluding remark
Part 3: Next step in HT measurements
Presentation Layout
Lund University/Dept. Energy Sciences/ Div. Heat Transfer /091202
Introduction
TMS are used in turbofan engines to guide the flow from the short-radius HPT to the large-radius LPT.
Typical turbofan (GP7000) engine with 4 sectionsTurbine section: High pressure turbine (HPT),Turbine Mid Structure (TMS), Low pressure turbine (LPT)
Lund University/Dept. Energy Sciences/ Div. Heat Transfer /091202
Introduction
Problem statement:TMS is located downstram of the HPT and it is exposed to very high heat loads.Cooling is needed to avoid leakage from the hot gas channel intothe domain surrounding the cold load carrying struture
Channel inlet
Leakage
The right the swirl flow with curved channel, ribs and jet injection.
outlet
Turbine section: HPT,TMS, LPT
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Basic approach & scope
Build a rather simple and easily changeable test rig (in HP stage cooling) Channel inlet
Curved channel flow
Jet injection
Rib
outlet
Flows of interest for cooling:
- Injection effects : feeding single/double confined jet- Surface disturbances: cylinder
ribs
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Objectives
To investigate :
Forced convective heat transferTurbulent flow
2 measurement techniques applied:
Liquid crystal thermography (LCT)Particle image velocimetry (PIV)
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Calibration of Wide-band Thermochromic Liquid Crystal (TLC R35C10W)
Part 2.1
ObjectiveTo demonstrate broader portion heat transfer distribution on thesurface in the channel flow combined with injection jet (s),multiple ribs, etc
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Liquid Crystal Thermography
TLC response to heating
PropertyThermochromic liquid crystal (TLC) change colors in response to temperature changes.ApplicationWhen TLC surface is illuminated with a white light source and heated through an active temperature range, it exhibits colors from red to blue through the visible color spectrum. This behavior is repeatable and reversible so that the TLC color can be calibrated directly as a function of temperature .
R35C10WLC with an event temperature 35 °C and color bandwidth of 10 °C.- Below event temperature, the LC appears transparent.- T rises through the bandwidth, LC turns R, G, and Bsequentially. - T exceeds the clearing point, LC reverts back to being transparent.
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Color interpretation
RGB ( red, green and blue)RGB defines a color
Human eye can not resolve the components of a color mixture
HSI ( Hue, saturation and intensity)HSI uses RGB concept to describe a color.
Hue- colorSaturation- purity of the colorIntensity- brightness of the color
Purple color is a mix of 56% red, 5% green, 61% blue
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Hue technique
In applications, R, G, B components of the image matrix are converted into H, S, I components.
Hue is directly related to the temperature
The relationship between hue and temperature is monotonic and hue is thus calibrated versus temperature.
Hue-temperature calibration curve is used to demonstrate the surface temperature distribution on the inner wall of the duct.
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Physical form : polyester sheet (Thin film of LC sandwiched between a transparent polymer substrate sheet and a black absorbing background)
Apparatus- 5 calibrated K-type thermocouples as reference to
calibrate LC.- Ordinary fluorescent lamp as a primary illuminant .- Image acquisition and software for image analysis
(CCD camera, PC, software, etc.)
Summary of Calibration
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
- Steady state calibration technique (TLC is set to pre-determined temperature within the color bandwidth and the image of the surface is acquired. The process is repeated through the bandwidth)
Pay efforts to capture images in steps of 0.5°C through the entire bandwidth.
-The calibration was conducted in situ, keeping identical optical arrangements as in the experiments.
Calibration Strategy
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Result: calibration curve
R35C5W hue-temperature feature
- The curve is fairly linear in the range of 35 °C to 37 °C.- The effective temperature range would be from 35 °C to 37 °C. - Resolution is 0.02 °C.
- Hue has a considerable sensitivity in the range of 36 °C to 41°C. - The effective temperature range would be the from 36°C to 43 °C .- Resolution is 0.1 °C .
R35C10W hue-temperature feature
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Part 2.2
Heat Transfer Measurement in Smooth Duct
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Test Rig
Downstream look towards the fan Air intake Suction fan
Test section, flexible walls
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Dimension of Thermal Rig
Inlet plane
Test section
Flow monitoring holes, top and side
Fan
Intake
3 m
1 m 1 m
inlet
250 [mm], wall S1
250 [mm], wall S2
250 [mm], wall S3
250 [mm], wall S480 [mm]
320 [mm]
outlet
Thermal test section
Heat transfer measurement is performed at the location of 3 m from the inlet duct where thermal B.L is fully developed.
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Heat foils
Liquid crystal strips
Sector 1
Sector 2
Sector 3
Sector 4
LC strips
Heating foil
LCT configuration ; S2 & S3
LCT configuration
Preparation: Thermal section (1)
Only one broader wall of the duct is electrically heated and the others are adiabatic.
LC strips are covered on the broader wall of the test section to demonstrate wall temperature distribution.
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
CCD
Lights
Thermal section
Adjust : illumination of primary lightsCCD camera
Primary disturbances:- Reflections from heating foil- Shades from different sources
Covering test window by a dark enclosure to prevent the interferencesfrom surrounding light
Preparation: Thermal section (2)
Thermal test section
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Test 1:HT measurements in Smooth Channel
Objective To measure the heat transfer (in terms of Nu) over the whole LC strip within the bandwidth in the measurement region:
Re = 10k-100k
Theory: Nu calculated from the Dittus-Boelter correlation with symmetric heating (1) and asymmetric heating correlation (2) :
Nu H = 0.023 Re H0.8. Pr 0.4 (1)
Nu H = 0.041 Re H0.727(2)
Experiment: Nu measured directly from heat flux and temperature difference:
Heat foil
TLC
Measurement region
A: area of heating surface (m2)kf : air thermal conductivity (W/m.K)
H: height of channel flow (m)
( )( ) AkTT
HQQNufbulkw
lossel
...
−−
=
νHum
H.Re =
Q el: measured input power to heater (W/m2)Q loss: heat loss by conduction (W/m2) Tbulk : air bulk temperature (K)Tw : surface temperature indicated by LC (K )
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Result: Re=10k‐100kExperimental condition : the temperature difference between surface and air bulk was kept within 13-15 °C.
Nusselt number in smooth duct
The consistency of the measured Nu with asymmetric heating correlation is clearly concluded.
R35C10W hue-temperature feature
Figure shows Nu distribution corresponding to green color region in the calibration curve.
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Theory: uncertainty analysis estimates how great an effect the uncertainties in the individual measurements have on the calculated result.
Experimental uncertaintiesElectric currentVoltage of heaterLC readingsAir bulk temperatureHeat loss by conduction
Heat loss (conduction)
k: thermal conductivity of Plexiglas (= 0.2 W/m. K)A: area of heating surface (m2)L: Plexiglas thickness∆T: temperature difference across the heated surface (three K-typed thermocouples)
The estimated uncertainty of Nu was within ± 8%
Uncertainty analysis
LTAkQloss
Δ= ..
( )( ) AkTT
HQQNufbulkw
lossel
...
−−
=
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Concluding remark
The consistency of the experimental data in the smooth duct by wide-band LCT gives confidence to pursue the effects of the confined jet with a shallow angle on convective heat transfer .
Lund University/LTH/ Energy Sciences/ Heat Transfer /091202
Next step
HT measurement in channel flow with single jet:U jet =35 m/s and Re = 100k
Heat foil
TLC
Measurement region