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Page 1: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t
Page 2: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

FEM in Heat TransferPart 2Part 2

Marcela B. Goldschmit

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Page 3: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

CONTENTS

Part 1Introduction to heat transferHeat transfer equationsNon-dimensional numbersThe finite element method in heat transferB d diti t l ti f d tiBoundary conditions: natural convection, forced convectionBoundary conditions: radiation, boilingExamples on conduction-convection heat transfer problems

Part 2Boundary conditions: reviewBoundary conditions: condensationBoundary conditions: condensationTime integrationNon-linear equations: Picard method, Newton-Raphson method, BFGSExamples on transitory thermal problems

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Examples on transitory thermal problems

Page 4: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

CONTENTS

Part 3Non-linear heat transferNon-linear heat transfer: thermal conductivity, forces term, volumetric termNon-linear heat transfer: radiation BCNon linear heat transfer: phase changeNon-linear heat transfer: phase changeModeling of heat transfer: weldingExamples on non-linear heat transfer problems

Part 4Inverse thermal problemsInverse thermal problemsExamples on phase change problems

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Page 5: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Boundary conditions: review

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Page 6: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Boundary conditions: review

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Page 7: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Boundary conditions: reviewNatural and Forced Convection

( )[ ]4

32

1

Pr/12

1

n

nn

n

A

RaAANu⎪⎭

⎪⎬⎫

⎪⎩

⎪⎨⎧

++=

( )[ ]Pr/1 3A ⎪⎭⎪⎩ +

Lh C/fkLhNu =

kCp

Cpkμ

ρρμ

==/

/PrPrGrRa =

( ) 3β LTT( )( )2

3

/ ρμβρ LTTGr w ∞−

=

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Page 8: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Boundary conditions: reviewB ili gBoiling

Nucleate

Boiling

Transition

Boiling

Film

Boiling

Free

Conv.

qcrit)

Boiling Boiling BoilingConv.

BCHF

log

(qs)

qmin C

A

MHF

log (ΔTe)

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Page 9: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Boundary conditions: condensation

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Page 10: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integration

( ) xQTktTCp Ω∈=∇⋅∇−∂∂ρ

xqq

xTTt

Tnn

Timp

impΤ∈=

Τ∈=∂

( ) conditioninitialTxT 00, =

( ) xHxtTxHtxT ˆ)(ˆ)(,~ ⋅=⋅=

( )( )

=Ω∇⋅∇−Ω∂∂

∫∫ ΩΩdTkHd

tTCpH TT ~~

ρ Part integration

( ) Τ−+Ω ∫∫ ΤΩdqqHdQH

qimpnn

TT

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Page 11: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integration

FTKTM =⋅+⋅•

ˆˆ

dBkBK

dhChM

G

jpie

Gij

e

Ω

Ω=

∫∑

∫∑Ω

ρ

kk

k ⎥⎥⎤

⎢⎢⎡

= 0000

hhhT

dBkBK

n

pjmpime

Gij

e

~21

⎥⎤

⎢⎡ ∂∂∂

⎥⎤

⎢⎡ ∂

Ω= ∫∑Ω

L niiG

i qhdQhF

k

∑∫∑∫ −Ω=

⎥⎥⎦⎢

⎢⎣ 00

TBT

hhhyh

yh

yh

xxx

yTx

n ˆˆ

~

~21 ⋅=⋅

⎥⎥⎥⎥⎥

⎢⎢⎢⎢⎢

∂∂∂∂∂

∂∂

∂∂

∂∂∂

=

⎥⎥⎥⎥⎥

⎢⎢⎢⎢⎢

∂∂∂

L

imp

q

ne

ie

ii qhdQh ∑∫∑∫ΤΩ

zh

zh

zh

zT n21 ⎥

⎦⎢⎢

⎣ ∂∂

∂∂

∂∂

⎥⎥⎥

⎦⎢⎢⎢

⎣ ∂∂ L

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Page 12: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integrationTime integration with convection therms

( ) QTkTvCTC pp =∇⋅⋅∇−∇⋅+∂ ρρ

( ) FTKNTM =⋅++⋅•

ˆˆ

( ) Qt pp ∂

ρρ

( ) FTKNTM =⋅++⋅

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Page 13: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integration

Time integration with convection therms

dBvhNdBkBK pjpi

eGijpjmpim

eGij ; Ω=Ω= ∫∫

ee∫∫ΩΩ

impnivi

eGi qhdqhF ∫∫ −Ω=

imp

eqe

nivii ∫∫ΤΩ

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Page 14: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integrationTime integration with convection therms

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Page 15: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integrationAlpha Method

( ) FTKNTM =++•

ˆˆ ( ) FTKNTM =⋅++⋅

The objective is to obtain an approximation for given the value of

and

Ttt Δ+ Tt

FF ttt Δ+

Alpha Method seeks to satisfy the differential equation in Alpha Method seeks to satisfy the differential equation in

10; ≤≤Δ+ αα tt

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Page 16: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integration: Alpha Method

( ) FTKNTM =⋅++⋅•

ˆˆ

tTTT

ttttt

Δ+•Δ+

Δ−

=αˆˆˆ

( ) ( ) TTttTTTT tttttt

ttt Δ+Δ+

Δ+ +−=Δ+Δ−

+= ααϑαα ˆˆ1ˆˆˆˆ 2( ) ( )

( ) FFF

ttt

ttttt Δ+Δ+ +

Δ

αα

ααϑα

α 1( ) FFF +−= αα1

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Page 17: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integration: Alpha Method

αααα

α

1=α Implicit Euler backward Method, unconditionally stable ( )tΔϑ

0=α Explicit Euler forward Method, conditionally stable

( )

( )tΔϑ

21

=α Implicit trapezoidal rule, unconditionally stableCranck Nicolson method

( )2tΔϑ

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2 Cranck Nicolson method

Page 18: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integration: Alpha Method

From Zienkiewicz & Taylor, The FiniteElement Method

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Element Method

Page 19: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integration: Alpha Method

Approximation error

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Page 20: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Time integrationPenetration depth measures the distance or thickness of thermal energy propagating into Penetration depth measures the distance or thickness of thermal energy propagating into the surface through conduction.

4 k

( ) 010

4

<−

=

initial

p

TT

tC

γ

ργ

is the minimum time at which temperature resultsare desired.

mint

( ) 01.0<− initialBC

initial

TTγ

N is the elements number to discriteze thepenetration depth

4 k

θTTipically N = 6 to 10

min4 t

Ck

Nx

pρ=Δ

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From Bathe, Finite Element Proceduresθ=TTipically N = 6 to 10

Page 21: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations

( ) RTF =ˆ ( ) RTTK =⋅ ˆSteady State

⎟⎠⎞⎜

⎝⎛=⎟

⎠⎞⎜

⎝⎛ Δ+Δ+Δ+ TRTTF

tttttttt ˆˆ,ˆTransient State ⎠⎝⎠⎝

( ) ( )TRTTTK tttttttt Δ+Δ+Δ+ =⋅ ˆ,

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Page 22: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Picard Method

It is called successive substitutions method.

Starting with an initial guess

Evaluate kk += 1( ) ( ) ( )TRTTTK

kktttktttktt Δ+Δ+−Δ+

=⋅⎟⎠⎞⎜

⎝⎛

+=

ˆ,ˆ

11

⎠⎝

Until the result no longer changes to within a specified toleranceUntil the result no longer changes to within a specified tolerance

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Page 23: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Picard Method

Picard's method is the easiest method to program and usually has large areas of convergence .g

Converges linearly and for many problems its convergence rate is very smooth

The most important application of Picard's method is to use it as the first iterations of the Newton-Raphson method .

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Page 24: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

Historical Note.

Newton's work was done in 1669 but published muchNewton s work was done in 1669 but published muchlater. Numerical methods related to the Newton Method were used by al-Kash, Viete, Briggs, and Oughtred, all many years before Newton.

Raphson, some 20 years after Newton, got close to Newton Equation, but only forpolynomials of degree 3, 4, 5, . . . , 10.

Raphson like Newton seems unaware of the connection between hisRaphson, like Newton, seems unaware of the connection between hismethod and the derivative. The connection was made about 50 years later(Simpson, Euler), and the Newton Method finally moved beyond polynomialequations. The familiar geometric interpretation of the Newton Method mayhave been first used by Mourraille (1768). Analysis of the convergence ofthe Newton Method had to wait until Fourier and Cauchy in the 1820s.

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Page 25: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

Steady state problem ( ) ( ) ( ) TTKTFTFR ˆˆˆ;0ˆ ⋅==−y p ( ) ( ) ( );0

( )1−∂

kFLinearized ( ) ( )

( ) ( ) ( )

,11 ;ˆ

ˆ =− Δ

∂∂

+= NEQjk

jj

k TTFFF

( ) ( ) ( )1ˆˆˆ −−=Δ kj

kj

kj TTT

iFK ∂Call tangent matrix

j

iT T

Kij ˆ∂

∂=

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Page 26: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

( ) ( ) ( )0ˆ11 =Δ⋅−− −− kkk TKFR 0=Δ⋅−−

TTKFR

( ) ( ) ( )11 ˆ −− Δ kkk FRTK ( ) ( )

( ) ( ) ( )1ˆˆˆ −−=Δ

−=Δ⋅kkk

T

TTT

FRTK

Start conditions( )

TT ˆˆ 0=Start conditions dataTT =

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Page 27: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

Transient state problem

TTKFFRtttttttttttt ˆˆ;0

Δ+Δ+Δ+Δ+Δ+Δ+ ⋅⎟⎠⎞⎜

⎝⎛==−

Linearized ( )( )

( ),1

1

1 ;ˆˆ =

Δ+

Δ+

Δ+−Δ+Δ+ Δ

∂∂

+= NEQjk

jtt

k

jtt

ttktttt T

TFFF

( ) ( ) ( )1ˆˆˆ −Δ+Δ+Δ+ −=Δ kj

ttkj

ttkj

tt

j

TTT

Call tangent matrixj

tti

tt

Ttt

TFK

ij ˆΔ+

Δ+Δ+

∂∂

=

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Page 28: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

( ) ( ) ( )0ˆ11 =Δ⋅−− Δ+−Δ+−Δ+Δ+ kttkttktttt TKFR 0Δ

TTKFR

( ) ( ) ( )11 ˆ −Δ+Δ+Δ+−Δ+ Δ kttttkttktt FRTK ( ) ( ) ( )

( ) ( ) ( )1

11

ˆˆˆ −Δ+Δ+Δ+

Δ+Δ+Δ+Δ+

−=Δ

−=Δ⋅kttkttktt

kttttttkT

tt

TTT

FRTK

Start conditions

( ) ( ) ( ) FFKKTT tttT

tT

ttttt=== Δ+Δ+Δ+ 000

;;ˆˆ

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Page 29: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

For one degree of freedom

( )1−kx( )kx

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Page 30: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

E l W th N t R h M th d t fi d l ti Example: We use the Newton-Raphson Method to find a non-zero solution of

x = 2 sinx

(a) Start x(0)= 1.1

(b) Start x(0)= 1.5

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Page 31: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

If the initial estimate is not close enough to the root, the Newton-RaphsonM h d h Method may not converge, or may converge to the wrong root.

The successive estimates of the Newton-Raphson Method may converge to the root too slowly, or may not converge at all.

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Page 32: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

T

T

( )1T̂Δ ( )2T̂Δ

Ttt ˆΔ+Tt ˆ Temperature

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Page 33: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

T

( )0T

tt

T

KTf

t

Δ+−=∂∂

T( )

( )1

1T

tt

T

KTf

tt

Δ+−=∂∂

Δ+

( )1T̂Δ ( )2T̂Δ Ttt ˆΔ+Tt ˆTemperature

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Ttt Δ+

Page 34: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

Convergence

Quadratic convergence when converges

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Page 35: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

Convergence

(1) First property

• If the tangent matrix is nonsingular( )1−Δ+ ktt K• If the tangent matrix is nonsingular

• If and its first derivatives with respect to are

TK

( )1−Δ+ ktt F( )1ˆ −Δ+ ktt

T

continuous in a neighborhood of the solution

• If will be closer to ( )1ˆ −Δ+ ktt

T *T̂

tt Δ+

*T̂

tt Δ+

• If will be closer to

than and the sequence of iterative solutions converges to

T T

( )kttT̂

Δ+ *T̂

tt Δ+

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Page 36: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Non-linear equations: Newton-Raphson Method

Convergence

(2) Second property – Lipschitz continuity

• If the tangent matrix satisfies( ) ( ) ( ) ( )11 ˆˆ −Δ+Δ+−Δ+Δ+ −≤−

kttkttkT

ttkT

tt TTLKK

for all in the neighborhood of

d L 0

( ) ( )1ˆˆ −Δ+Δ+ kttkttTandT

*T̂

tt Δ+

and L>0

then convergence is quadratic.

This means that if the error after iteration (k) is the order e, then the error after iteration (k+1) will be of the order e2

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Page 37: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Modified Newton-Raphson Method

N-R iteration is recognized as an expensive computational cost per iteration due

to the calculation and factorization of the tangent matrix. Then, the use of a

modification of the full N-R algorithm can be effective.

Maintains the o tangent matrix constant during the iterations or

it is modified each n iterations

( )1−Δ+ kT

tt K( )xf '

Advantage: saving computational effort

Disadvantage: loss of quadratic convergence g q g

The choice of time step depend on the degree of non-linearities

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Page 38: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Quasi-Newton Methods: BFGS

As an alternative to forms of N-R iteration, a class of methods known as matrix update methods or quasi-Newton methods has been developed .

These methods involve updating the coefficient matrix to provide a secantapproximation to the matrix from iteration (k-1) to (k).

BFGS: Broyden, Fletcher, Goldfarb and Shanno method

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Page 39: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Quasi-Newton Methods: BFGSInicialize las

k = k+1

Inicialize lasmatrices y vectores, 

k=0

k = k+1

t+∆t∆T(k) = (t+∆tKT‐1)(k‐1)  . (t+∆tR ‐ t+∆tF(k‐1)) 

Calcular t+∆tF(k)( t+∆tT(k) )

(t+∆tKT‐1)(k) = A(k)T . (t+∆tKT‐1)(k‐1) . A(k)t+∆tT(k) =  t+∆tT(k‐1) + t+∆t∆T(k)

F ( T )

Converge en alguna  nonorma

siSiga con el paso 

de tiempo sig iente

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de tiempo siguiente

Page 40: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Quasi-Newton Methods: BFGS

(k)T( )TkA( )kA

TT

TTT T

TTT

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Page 41: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Quasi-Newton Methods: BFGS

( ) ( ) ( )

( ) ( ) ( )1

1ˆˆˆ−Δ+Δ+Δ+

−Δ+Δ+Δ+

Δ

−=Δkttkttktt

kttkttktt

FFF

TTT( ) ( ) ( )1Δ+Δ+Δ+ −=Δ kttkttktt FFF

Since the product( )kA( )TkA

is positive definite and symmetric, to avoid numerically problems, the condition number is calculated.

The update is performed if:( ) ( )510=< nexampleasnc k

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Page 42: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

BFGS with linear searches ( ) ( ) ( )1ˆˆˆ −Δ+Δ+Δ+ Δ

kttkttktt TTT β( ) ( ) ( )Δ+ −=Δtt TTT β

b is a scalar multiplier

It is varied until the component of the out-of-balance loads in the

direction is small.( )ktt T̂ΔΔ+ TΔ

( ) ( )( ) ( ) ( )( )1ˆˆ −Δ+Δ+Δ+Δ+Δ+Δ+ Δ−ΔΔ≤Δ−ΔΔ kttttTkttktttt

Tktt FRTTOLFRT ( ) ( )O

Linear searches are made with simple algorithms such as bisection

Linear searches are computationally expensive because they must calculate multiple times in each iteration ( )ktt FΔ+

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Page 43: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

BFGS with linear searches Inicialize las

k = k+1

matrices y vectores, k=0

t+∆t∆T(k) = (t+∆tKT‐1)(k‐1)  . (t+∆tR ‐ t+∆tF(k‐1)) 

Calcular t+∆tF(k)( t+∆tT(k) )

(t+∆tKT‐1)(k) = A(k)T . (t+∆tKT‐1)(k‐1) . A(k)t+∆tT(k) =  t+∆tT(k‐1) +β t+∆t∆T(k)

Converge en alguna norma

no

siSiga con el paso 

de tiempo siguiente

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Page 44: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Convergence criteria

1) Convergence in temperatures ( )DTOLT

ktt <ΔΔ+ ˆ

2) Convergence in porcentual values

( )

( ) ETOLT

ktt

ktt

−Δ

Δ+

ˆ

( )T

ktt ΔΔ+ 1

( ) in

i

in

i

i aaaaaa max;;1

11

2

2===

∞==∑∑

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Page 45: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Examples on transitory heat transfer problemsExercise 1: Obtain the FEA formulation for the Linear Transitory heat transfer problem

considering convection. Analyze the stability of the different timeintegration

Exercise 2: Consider the transitory heat transfer problem in a 1D beam discretizedy pwith 10 regular elements. Solve the finite element model with time integration for different alpha values (0; 0.5 and 1) for the following cases:

Heat transfer equation

Border Condition

Initial Condition

Use this non-dimensional numbers for the analysis:

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Page 46: FEM in Heat Transfer Part 2 · CONTENTS Part 1 Introduction to heat transfer Heat transfer equations Non-dimensional numbers The finite element method in heat transfer B d diti t

Examples on transitory heat transfer problems

Exercise 3: Consider a 90º semi-infinite cylinder. Sides AB and BC are subjected to prescribed temperature of 50º. The initial temperature profile is 0º. The heat capacity of the material is constant. Perform a transient analysis to calculate the temperature distribution within the semi infinite domain at different values of time Use the Euler distribution within the semi-infinite domain at different values of time. Use the Euler Backward, Cranck Nicholson and Euler Forward Method.

The domain is discretized using a 10 × 10 mesh of 4 node 2 D conduction elementsof 4-node 2-D conduction elements.The conduction matrix is evaluated using a consistent heat capacity matrix. The timestep is Δt = 0.016.

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