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Surface Heat Transfer In Quenching Operations

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To develop a module for calculating the surface heat transfer coefficient (HTC) ... Time Variable number of future temperatures ( Blanc, G 1997) ... – PowerPoint PPT presentation

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Title: Surface Heat Transfer In Quenching Operations


1
Surface Heat Transfer In Quenching Operations
Research Team Kalyana C. Gummadam
gummkal_at_iit.edu T Calvin
Tszeng
tszeng_at_iit.edu
Thermal Processing Technology Center Department
of Mechanical, Materials and Aerospace Engineering
2
Outline
  • OBJECTIVES STRATEGY
  • OVERVIEW OF QUENCHING BACKGROUND
  • FEM MODEL
  • EFFECT OF T/C LOCATION TIMESTEP SIZE
  • STABILITY ACCURACY
  • EFFECT OF NOISE
  • TIME LAGGING
  • CONCLUDING REMARKS/ FUTURE RESEARCH

3
OBJECTIVES
  • To develop a module for calculating the
    surface heat transfer coefficient (HTC) which is
    to be used in the FEM modeling of components in
    the quenching operations of industrial heat
    treating processes.
  • To develop the reliable methodology for
    determining the surface heat transfer
    coefficients from measured temperature profiles
    in quenched specimens.
  • To develop an efficient temperature sensing
    strategy and experimental method, and to measure
    the temperature profiles in quenched specimens.

4
STRATEGY
  • Perform extensive study on the inverse heat
    transfer module in the 2D modeling system
    HOTPOINT. Determine the influence of various
    factors on the solution behavior
  • Develop an efficient and reliable
    technique of temperature measurement that
    provides the data for determining the surface
    heat transfer coefficients.
  • Establish a neural network model for
    predicting the surface heat transfer coefficients
    in a broad range of quenching operations

5
OVERVIEW OF QUENCHING
Wetting process on the surface of a 1040 steel
Adopted form     George E. Totten, Maurice A.H.
Howes, Steel Heat Treatment Handbook, 1997
6
BACKGROUND
  • Inverse Heat Transfer
  • Fourier law for heat flux through the surface
    ---
  • Determination of the boundary conditions (heat
    transfer coefficients) that aaproduce a
    specified, or measured , internal temperature
    distribution.
  • Underlying mathematical problem is ill-posed
  • Solution does not depend continuously on the
    data
  • Small errors in the data may cause large errors
    in the solution
  • Various Approaches
  • Conjugate Gradient method( Huang, 1999)
  • Time Variable number of future temperatures (
    Blanc, G 1997)
  • Space Marching Algorithm( Al-Khalidy, 1998)
  • Sequential Methods( Reinhardt, 1993)
  • Function Specification method ( Beck, 1985)

7
INVERSE CALCULATION
  • 2D FEM MODEL HOTPOINT 1.0 ( T Calvin Tszeng,
    IIT)

Mesh the Object
Specify HTC at object surfaces
Location of T/Cs
Perform Direct Simulation
Generate Cooling curves
Perform Inverse Calculation
Generate Surface HTC
Error Analysis
8
VALIDATION
  • The inverse heat transfer module can offer
    generally good results of surface heat transfer
    coefficients by using the simulated cooling
    curves.
  • Time step size that is greater than the sampling
    rate of cooling curves can reduce instability in
    the results.
  • The oscillation in the solution can be reduced by
    using a regulating parameter which is
    incorporated in the residual error function.

9
EFFECT OF SENSOR LOCATION
1D Axi Symmetric Initial temperature 1200
C Quenching time 40 s
Insulated
dx
Heat Transfer
10
EFFECT OF SENSOR LOCATION
Time step size 0.4s Regulating parameter of
0.75
  • Good accuracy until a depth of 5mm
  • Deviation from the true solution at higher depths

11
EFFECT OF TIMESTEP SIZE
dx 10mm Regulating parameter 0.75
  • Better accuracy at larger time step size under
    2s
  • Bad solution at much higher time step size due
    to insufficient data
  • Time lag reduces the accuracy at smaller time
    step size

12
STABILITY AND ACCURACY (1/3)
Symbolic Mathematical Model F A ?B Error
Equation A (dT)2 -- Temperature Error (
Stochastic) B (dh)2 -- Solution Error (
Deterministic) ? Regulating Parameter (
Numerical Const)
Insulated
  • 1D Case Considered
  • Axi-symmetric geometry.

h(T)
Heat Transfer
13
STABILITY AND ACCURACY (2/3)
  • Varying regulating parameter (0.01-100) after
    different times Initial regulating parameter
    value of 0.75
  • Accuracy decreases with increase in regulating
    parameter
  • Accuracy and stability both decrease with
    further increase in regulation parameter value

After 2.5s
Stability
2
After 7.5s
Stability
14
STABILITY AND ACCURACY (3/3)
OD- 1.5 Length - 6 h heat transfer
co-efficient
  • 2D Case
  • Axi-symmetric geometry.

l
0.01
  • After 2.5 s
  • Similar results as compared
  • to 1D case
  • Good Stability for all ?
  • values
  • Accuracy decreases as ?
  • increases

0.008
2
2
5
5
0.006
100
0.004
20
20
0.002
0
0
2
4
6
8
10
15
EFFECT OF NOISE
  • Constant Boundary condition
  • 10 peak to peak noise induced
  • Sequential Digital filter algorithm used to
    smooth data
  • Smoothed data provides better results

with 10 noisy data
with smooth data
theoretical solution
16
TIME LAGGING (1/4)
Temperature Calculations




T

, t

, x

  • Constant Heat flux applied to semi infinite body
  • T -- Dimensionless Temperature
  • t -- Dimensionless time
  • x -- Dimensionless distance

Adopted from Beck,J.V 1992
17
TIME LAGGING (2/4)
10 mm
15 mm
20 mm
25 mm
  • Normalized Second derivative of the Temperature
    Vs Time
  • Obtain points of inflection for increasing dx
    (T)
  • Time lag increases with distance

18
TIME LAGGING (3/4)
surf
Reference line
1000
  • The deviation from the cooling curve for a
    change in the boundary condition can be
    distinctly seen
  • Time lag increases with distance
  • Time lag beyond 5mm is substantial

19
TIME LAGGING (4/4)
  • Linear relation between Theoretical and
    Calculated time lag
  • For 1D case the calculated time lag can be
    estimated from this plot
  • The time lag could specify the min time step
    size to be used
  • A closed form solution for the theoretical case
    will

20
SUMMARY ( 1/2)
  • Sensor Location
  • Deviation from the true solution at higher
    depths
  • Good accuracy for Sensor location until a depth
    of 5mm
  • Time step size
  • Bad solution at much higher time step size due
    to insufficient data
  • Instability arises at very small time step size
  • The choice of time step size depends on the
    location of sensor
  • Regulating Parameter
  • Solution accuracy and stability become poorer
    for higher values of aaregulation
    parameter.
  • Lower regulating parameter leads to better
    accuracy and stability

21
SUMMARY ( 2/2)
  • Noise
  • More the noise, more inaccurate and unstable the
    solution
  • Sequential Digital Filter Algorithm used to
    smooth the data
  • Time Lag
  • Poor accuracy at small time step size due to
    time Time lag
  • Time lag increases with distance and is
    substantial beyond 5mm
  • Time lag Provides an estimate of minimum time
    step size to be aaused to obtain a better
    solution
  • Future Research

22
NEXT STEPS(1/2)
Experimentation
Material - 1045 Cold Rolled Geometry -
Solid Rounds Furnace - IIT Samples
- Diameter Length 1 8,6,4,2,1,0.5 2 12,
8,6,4,2,1,0.5 - 12 TCs (max) on each
sample. -Measure cooling curves at different
locations on the surface - Perform Inverse
calculation to obtain HTCs
23
NEXT STEPS(2/2)
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