on optimal control problems in radiative · pdf fileduring the last years optimal control and...

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On Optimal Control Problems in Radiative Transfer Michael Herty * Rene Pinnau Mohammed Sea¨ ıd October 10, 2005 Abstract Optimal control problems for the radiative transfer equation are introduced and formulated. We consider as control variable a source term in the radiative transfer equation. Necessary and sufficient optimality conditions are derived and discussed. Numerical methods for the model equation and its adjoint are presented. Especially, the discrete ordinates method and finite volume discretization are formulated for two- dimensional problems. Computational results based on a steepest descent method are given for two test examples underlining the feasibility of our approach. Keywords. Radiative transfer, Optimal control, First–Order Optimality, Discrete ordinates, S N -equations, Iterative methods. 1 Introduction During the last years optimal control and inverse problems for radiative heat transfer gained considerable attention in many fields of application, e.g. the cooling of glass, gas turbine combustion chambers or combustion in car engines [4, 23, 17, 16, 15]. These pose several challenging problems from the simulation point of view and even more challenging concerning the optimization, which have to be encountered by engineers and applied math- ematicians. The reason is the high numerical complexity of the model equations which are given by the radiative heat transfer system for the radiative intensity. This led to the development of a whole hierarchy of approximative equations, ranging from moment expansion to diffusive type models, like the SP N –systems [10, 9]. Due to the high dimensionality of the phase space of the discretized radiative transfer equation, most optimization approaches are based on approximate models coupled with a heat equation. These approaches allow to compute optimal controls at reasonable numer- ical costs. Nevertheless, there are applications in which one needs the detailed knowledge of the radiative intensity, like strongly scattering or optically thin media [14]. Then, the mentioned approximate models are no longer appropriate and one has to go back to the full radiative transfer equation (RTE). In this paper we will introduce and discuss optimal control problems for the multidimensional RTE including scattering. Especially, we develop a numerical study for optimal control problems of tracking–type in radiative transfer where the cost functionals have the form F (R, Q) := α 1 2 Z D ( R - ¯ R ) 2 dx + α 2 2 Z D ( Q - ¯ Q ) 2 dx. * Fachbereich Mathematik, Technische Universit¨ at Kaiserslautern, D–67663 Kaiserslautern, Germany ([email protected]) Fachbereich Mathematik, Technische Universit¨ at Kaiserslautern, D–67663 Kaiserslautern, Germany ([email protected]) Fachbereich Mathematik, Technische Universit¨ at Kaiserslautern, D–67663 Kaiserslautern, Germany ([email protected]) 1

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Page 1: On Optimal Control Problems in Radiative · PDF fileDuring the last years optimal control and inverse problems for radiative heat transfer ... gas turbine combustion chambers or combustion

On Optimal Control Problems in Radiative Transfer

Michael Herty∗ Rene Pinnau† Mohammed Seaıd‡

October 10, 2005

Abstract

Optimal control problems for the radiative transfer equation are introduced andformulated. We consider as control variable a source term in the radiative transferequation. Necessary and sufficient optimality conditions are derived and discussed.Numerical methods for the model equation and its adjoint are presented. Especially,the discrete ordinates method and finite volume discretization are formulated for two-dimensional problems. Computational results based on a steepest descent method aregiven for two test examples underlining the feasibility of our approach.

Keywords. Radiative transfer, Optimal control, First–Order Optimality, Discreteordinates, SN -equations, Iterative methods.

1 Introduction

During the last years optimal control and inverse problems for radiative heat transfergained considerable attention in many fields of application, e.g. the cooling of glass, gasturbine combustion chambers or combustion in car engines [4, 23, 17, 16, 15]. These poseseveral challenging problems from the simulation point of view and even more challengingconcerning the optimization, which have to be encountered by engineers and applied math-ematicians. The reason is the high numerical complexity of the model equations whichare given by the radiative heat transfer system for the radiative intensity. This led tothe development of a whole hierarchy of approximative equations, ranging from momentexpansion to diffusive type models, like the SPN–systems [10, 9].

Due to the high dimensionality of the phase space of the discretized radiative transferequation, most optimization approaches are based on approximate models coupled with aheat equation. These approaches allow to compute optimal controls at reasonable numer-ical costs. Nevertheless, there are applications in which one needs the detailed knowledgeof the radiative intensity, like strongly scattering or optically thin media [14]. Then, thementioned approximate models are no longer appropriate and one has to go back to thefull radiative transfer equation (RTE). In this paper we will introduce and discuss optimalcontrol problems for the multidimensional RTE including scattering.

Especially, we develop a numerical study for optimal control problems of tracking–typein radiative transfer where the cost functionals have the form

F(R, Q) :=α1

2

D

(R− R

)2dx +

α2

2

D

(Q− Q

)2dx.

∗Fachbereich Mathematik, Technische Universitat Kaiserslautern, D–67663 Kaiserslautern, Germany([email protected])

†Fachbereich Mathematik, Technische Universitat Kaiserslautern, D–67663 Kaiserslautern, Germany([email protected])

‡Fachbereich Mathematik, Technische Universitat Kaiserslautern, D–67663 Kaiserslautern, Germany([email protected])

1

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Here, R(x) :=∫Sd I(ω.x)dω is the mean intensity and the radiative intensity I is given as

the solution of the RTE. The variable of interest to be controlled is the source term Q,which can be interpreted as a gain or loss of radiant energy deployed by external forces.

Using the adjoint calculus we derive the first–order optimality condition and prove theexistence of an optimal control. We use this first–order derivative information to devise agradient method for the numerical optimization.

The paper is organized as follows. In the remainder of this section we recall the RTEused in the current work. Then, in Section 2 we formulate the optimal control problemassociated with the considered RTE and derive the first–order optimality condition. Weprove the existence of adjoint states and deduce the existence of an optimal control. InSection 3 we describe the steepest descent method and give an appropriate discretizationfor the optimal control problem. We present two numerical examples, source inversionand edging, in Section 4, which underline the feasibility of our approach.

1.1 The Radiative Transfer Equation

Radiative transfer equations can be written in general form [14, 13] as

∀ ν > ν0 :1c

∂I∂t

+ ω · ∇I + (σ + κ)I =σ

Sd

Idω + κB(θ, ν), (1.1)

where I(t, ν, ω,x) is the spectral intensity at time t, in position x, within frequency ν andpropagating along direction ω with a speed c. In (1.1), Sd denotes the unit sphere in Rd,θ is the temperature, κ = κ(ν,x) is the absorption coefficient, σ = σ(ν,x) is the scatteringcoefficient, ν0 is the upper bound of opaque band of the optical spectrum where radiationis completely absorbed, and B(θ, ν) is the spectral intensity of the black-body radiationgiven by the Planck function

B(θ, ν) =2hν3

c20

(ehν/kθ − 1

)−1, (1.2)

where h, k and c0 are Planck’s constant, Boltzmann’s constant and the speed of radia-tion propagation in vacuum, respectively, compare [13] for further physical details. Formathematical aspects of the radiative transfer equation and related issues see for instance[14]. We note that isotropic scattering media has been considered in (1.1) however, allthe results presented in this paper can be straightforwardly extended to radiative transferproblems in non-isotropic scattering media.

The equations (1.1) are solved subject to the boundary condition

I(t, ν, ω,x) = %(n · ω)I(t, ν, ω′,x) + (1− %(n · ω))B(θb, ν), n · ω < 0, (1.3)

where % ∈ [0, 1] is the reflectivity: % = 1 for total reflection and % = 0 for Dirichlet typeboundary conditions. The temperature θb is a fixed boundary function, n is the outwardnormal on the boundary and ω′ = ω − 2(n · ω)n is the specular reflection of ω on theboundary. Initial condition is supplied to (1.1) as

I(0, ν, ω,x) = I0(ν, ω,x), (1.4)

with I0(ν, ω,x) is a given function. For sake of simplicity, we shall consider the followingradiative transfer model

ω · ∇I + (σ + κ)I =σ

Sd

Idω + Q,

(1.5)I(ω,x) = A, n · ω < 0,

2

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where Q is the source term and A is a given boundary data.

Even so we assume severe simplifications, these equations are still reasonable in manyapplications, e.g. when dealing with grey medium and if the mean free path of the radiationis small compared to a characteristic length.

2 Optimal Control Problems in Radiative Transfer

In this section we give the precise mathematical setting of the optimal control problemand derive the first–order optimality conditions. Especially, we prove the existence of anunique optimal control. The ideas follow results of [7]. However, the considered functionspaces as well as in the additionally treatment of optimal control problems is new.

Results on optimal control problems in the one-dimensional case are reported in [1].In contrast to [1], we deal with multi–dimensional problems and distributed controls, butwe do neglect heat transfer.

Different optimal control problems related to heat transfer are also discussed in [12].

2.1 The Optimal Control Problem

We consider an optimal control problem for a general objective function of trackingtype (2.2). Then, we derive the first order optimality conditions and give existence anduniqueness results for the optimality system.

In the following, we assume that x ∈ D ⊂ Rd, d = 2 or 3. To avoid technical difficultieswe assume that D is a bounded domain with Lipschitz boundary. We introduce a convex,tracking-type objective function of type depending on the mean intensity (also called”radiosity”)

R(x) :=∫

Sd

I(x, ω)dω. (2.1)

Furthermore, we denote distributed control by Q(x) and we define the functional F as

F(R, Q) :=α1

2

D

(R− R

)2dx +

α2

2

D

(Q− Q

)2dx, (2.2)

with positive constants α1, α2 and given (desired) states and controls R and Q, respectively.

The general optimal control problem reads

minR,Q

F(R, Q) subject to (1.5) and (2.1). (2.3)

with function spaces for R and Q defined below.

Formally, the partial differential equation (2.4) for the adjoint function J(ω,x) is givenby

−ω · ∇J(ω,x) + (σ + κ)J(ω,x) =σ

Sd

J(ω,x)dω + α1

(R(x)− R(x)

),

(2.4)J(ω,x) = 0, n · ω > 0.

and the gradient equation (or optimality condition) is given by

α2

(Q(x)− Q(x)

)+

Sd

J(ω,x)dω = 0. (2.5)

3

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2.2 Adjoint Calculus

We now give a rigorous derivation of the adjoint and gradient equation. First and asin [7], we reformulate the state equation (1.5) of the optimal control problem: Let D bea bounded domain and let A be constant boundary data for ingoing directions ω. For afixed x ∈ D and a fixed direction ω ∈ Sd we denote by p(ω) ∈ ∂D the point, where thedirection ω meets the boundary of D for the first time and such that xp(ω) is parallel toω, see Figure 2.1.

D

x

p(ω)

ω

Figure 2.1: Domain D and the points x and p(ω) for the two-dimensional problem.

For fixed (ω,x) ∈ Sd ×D we integrate (1.5) along the line–segment p(ω)x and obtainan (implicit) equation for R(x) :

R(x) = A

Sd

exp

(−

∫ x

p(ω)(σ + κ)ds

)dω +

Sd

∫ x

p(ω)exp

(−

∫ x

r(σ + κ)ds

) ( σ

4πR(r) + Q(r)

)drdω. (2.6a)

Note, that the integrals are path integrals along line–segments. Therefore, and if weassume σ and κ to be constant on D,

∫ x

p(ω)(σ + κ)ds = ‖x− p(ω)‖2(σ + κ). (2.7)

Moreover, there exists a coordinate transformation, such that the integrals in (2.6) can begiven in Euclidean coordinates: Consider a fixed point x in the interior of D and a fixeddirection ω ∈ Sd. Then, a parametrization of the line–segment p(ω)x is given by

t 7→ γ(t; ω, x) = x− tω, γ : [0, cω] −→ p(ω)x,

for some constant cω. For each y in the interior of D and y 6= x, we find a unique pair(ω, t) such that

γ(ω, t) = y and t ≤ cω.

Hence, the transformation Φ : {(ω, t) : ω ∈ Sd, t ∈ [0, cω]} → D is well–defined. Thetransformation formulas yield in the multi-dimensional case (see also [7])

d = 2 :∫

S2

∫ x

p(ω)F (r)drdω =

D

F (y)‖x− y‖2

dy, (2.8)

d = 3 :∫

S3

∫ x

p(ω)F (r)drdω =

D

F (y)‖x− y‖2

2

dy. (2.9)

4

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Second, we prove some properties of the kernel of equation (2.6). Lemma 1 is similarto [7] and changed only to incorporate our the two–dimensional case and our boundarycondition.

Lemma 1 Let d = 2. Assume σ, κ > 0 to be constant on a bounded domain D. Define thekernel k(x, y) : D ×D → R by

k(x,y) = σexp (−(σ + κ)‖x− y‖2)

4π‖x− y‖2. (2.10)

Then the following holds true.

(i) k(·,y) ∈ L1(D), k(x,y) = k(y,x) and k ≥ 0.

(ii) The operator K : Lp(D) → Lp(D) given by

K(f)(x) =∫

Sd

∫ x

p(ω)

σ

4πexp

(−

∫ x

r(σ + κ) ds

)f(r)drdω, (2.11)

is well-defined for 1 ≤ p < ∞.

(iii)∫D K(f)(x)dx =

∫D K(1)(x)f(x)dx for all f ∈ Lp(D), 1 ≤ p < ∞.

(iv) ‖K‖Lp(D),Lp(D) ≤ 1 for 1 < p < ∞ and (I −K) : Lp(D) → Lp(D) is an invertibleoperator.

Proof.

Obviously, k is symmetric and non-negative. Using the coordinate transformationintroduced above, we see, that k(·,y) ∈ L1(D). Next, we prove that K maps Lp(D) toLp(D). Consider f ∈ L1(D), then by Fubini’s theorem

D|K(f)|(x)dx =

D×Dk(x,y)|f(y)|dydx,

=∫

D|f(y)|

Dk(x,y)dxdy < ∞. (2.12)

Equation (2.12) also reveals property (iii). Further, for f ∈ Lp(D), 1 < p < ∞ we obtainby Holder’s inequality for 1/p + 1/q = 1:

D|K(f)(x)|pdx =

D

(∫

Dk(x,y)

1p+ 1

q |f(y)|dy)p

dx

≤∫

D

(∫

Dk(x,y)|f(y)|pdy

)(∫

Dk(x,y)dy

)p/q

dx

≤ cp/q2

DK(|f |p)(x)dx

≤∫

D|f(y)|p

Dk(x,y)dxdy

≤ cp/q+12 ‖f‖p

Lp(D) < ∞,

where c2 =∫D k(x,y)dy. The above calculation yields ‖K‖Lp(D),Lp(D) ≤ 1, once we proved

5

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that c2 ≤ 1.

Dk(x,y)dy =

D

σ

exp(−σ‖x− y‖2)‖x− y‖ exp(−κ‖x− y‖2)dy

≤∫

D

σ

exp(−σ‖x− y‖2)‖x− y‖2

dy

=∫

S2

14π

∫ x

p(ω)exp(−σ‖x− r‖2)σdrdω

=∫

S2

14π

exp (−σ‖x− r‖2) |r=xr=p(ω)dω

≤ 14π

S2

1 dω

≤ 12.

This finishes the proof.

Remark 1 Lemma 1 remains true in the case d = 3, if we replace the kernel k(x,y) by

k(x,y) = σexp(−(σ + κ)‖x− y‖2)

‖x− y‖22

.

Then one obtains c2 ≤ 1 and again ‖K‖Lp(D),Lp(D) ≤ 1.

Remark 2 In fact, Lemma 1 is an existence theorem for equation (2.6). Indeed, let usrewrite (2.6) as

R(x) = c1 + K(R)(x) + K

(4π

σQ

)(x), (2.13)

with the constant

c1 := A

Sd

exp

(−

∫ x

p(ω)(σ + κ)ds

)dω. (2.14)

Then, for Q ∈ Lp(D), we obtain from Lemma 1 the unique solution to (2.13) as

R = (Id−K)−1

(c1 + K

(4π

σQ

)(x)

). (2.15)

If σ ∈ L∞(D), we consider the weighted Lp−space

Lpσ(D) :=

{f :

Dfp(y)σ(y)dy < ∞

}

and define K : Lpσ → Lp

σ to proceed analogously to Lemma 1. For our purposes the case σand κ constant, is sufficient.

Finally and with all the previous remarks in mind, we can state the optimal controlproblem. Due to Remark 2 and Lemma 1, the following reformulation of the optimalcontrol problem (2.3) is well–posed. Let d = 2 or 3 and R, Q ∈ L2(D) are given functions,

minR,Q∈L2(D)

α1

2

D

(R(x)− R(x)

)2dx +

α2

2

D

(Q(x)− Q(x)

)2dx, (2.16)

6

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subject to

R(x) = A

Sd

exp

(−

∫ x

p(ω)(σ + κ)ds

)dω +

Sd

∫ x

p(ω)exp

(−

∫ x

r(σ + κ)ds

) ( σ

4πR(r) + Q(r)

)drdω. (2.17)

Now, we are able to derive the necessary optimality conditions for (2.16). Let,

H(R, Q) := (Id −K)R− c1 −K

(4π

σQ

): L2(D)× L2(D) → L2(D),

where Id denotes the identity matrix in Rd. Obviously, for all R, Q ∈ L2(D), the operatorH′ is linear and bounded, i.e.,

H′(R, Q) ∈ L(L2(D)× L2(D);L2(D)

).

Moreover, for any f ∈ L2(D) and all R, Q ∈ L2(D) the pre-image

(Rf , Qf ) =(f,− σ

4πf)

satisfiesH′(R, Q)[Rf , Qf ] = f.

Here and from now A[x] represent the application of the linear operator A to x. The abovecalculations show, thatH′ is a surjective operator defined on L2(D)×L2(D). Therefore, wecan apply the Lagrange Multiplier Theorem to derive the necessary optimality conditions.To be more precise, due to [11][Theorem 1, p243], there exists a function λ∗ ∈ L2(D)∗,which we identify with λ ∈ L2(D), such that the necessary first–order optimality condi-tions (2.18) are satisfied in a local minimum (R0, Q0). Moreover, since F is convex, theseconditions are also sufficient.

F ′(R0, Q0)[R, Q]−∫

Dλ(x)H′(R0, Q0)[R, Q](x)dx = 0, ∀ R,Q ∈ L2(D), (2.18a)

H(R0, Q0) = 0, a.e. x ∈ D. (2.18b)

Next, we verify the formal calculations by further discussion of properties of the first orderoptimality system (2.18).

Using the variational lemma we deduce from (2.18a)

α1

(R0 − R

)− (Id−K∗)λ = 0, a.e. x ∈ D, (2.19a)

α2

(Q0 − Q

)+

σK∗λ = 0, a.e. x ∈ D, (2.19b)

where K∗ : L2(D) → L2(D) is the adjoint operator to K. K is self–adjoint, since inEuclidean coordinates we have:

Dg(x)K(f)(x)dx =

D

Dg(x)k(x,y)f(y)dydx,

=∫

D

Dg(x)k(y,x)f(y)dydx,

=∫

DK(g)(y)f(y)dy.

7

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Furthermore, since λ satisfies the above system we conclude that there exists a function

P (x) :=4π

σK∗ (λ(x)) ∈ L2(D),

which satisfies

α14π

σK∗ (

R0 − R)− (Id −K∗)P = 0, a.e. x ∈ D, (2.20a)

α2

(Q0 − Q

)+ P = 0, a.e. x ∈ D. (2.20b)

The condition (2.20) is necessary for optimality but not sufficient, since in general K∗

is not invertible. An equation for P will be used to justify the formal computations inthe beginning. From the first equation in (2.20) we derive the equivalent reformulation inEuclidean coordinates

P (x) =∫

Dk(x,y)

(P (y) + α1

σ

(R0(y)− R(y)

))dy. (2.21)

Now, we justify the formal calculations in the first section: For fixed ω ∈ Sd denote byp∗(ω) the point on ∂D where the direction ω leaves D. In contrast to the previous dis-cussion we consider path–integrals along the line–segment xp∗(ω) and its parametrization

t 7→ γ∗(t;x, ω) := x + tω, γ : [0, c∗ω] −→ xp∗(ω)

for some constant c∗ω and fixed ω ∈ Sd, see Figure 2.2. Again, for each y 6= x in theinterior of D we find a unique (t, ω) such that

γ∗(t, ω) = y

and t ≤ c∗ω. This defines a transformation Φ∗ from D to {(t, ω) : ω ∈ Sd, 0 ≤ t ≤ c∗ω}.

D

x

ω

p*(ω)

Figure 2.2: Domain D and the points x and p∗(ω) for the two-dimensional problem

Applying the transformation Φ∗ to (2.21) we obtain

P (x) =∫

Sd

∫ x

p∗(ω)exp

(−

∫ x

r(σ + κ)ds

)( σ

4πP (r) + α1

(R0(r)− R(r)

))drdω. (2.22)

Equation (2.22) is the reformulation of

−ω · ∇J(ω,x) + (σ + κ)J(ω,x) =σ

Sd

J(ω,x)dω + α1

(R0(x)− R(x)

),(2.23a)

J(ω,x) = 0, n · ω > 0, (2.23b)

8

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provided that

P (x) =∫

Sd

J(ω,x)dω.

Here, J(x, ω) is the solution to equation (2.23). This follows from (2.24), (2.22), Remark 3(see below) and the definition of Φ∗.

Remark 3 Using the definitions above, we derive for a differentiable function F and afixed direction ω, the following equation (2.24).

∫ x

p∗(ω)−ω · ∇F (s, ω)ds = F (x, ω)− F (p∗(ω), ω). (2.24)

We summarize the calculations above as final result of this section.

Theorem 1 Given a bounded domain D ∈ Rd with d = 2 or 3. Let positive constantsα1, α2 and functions R, Q ∈ L2(D) be given. Consider the optimal control problem (2.16).

Then, there exists a function λ ∈ L2(D), such that the necessary and sufficient firstorder optimality conditions for (2.16) are as follows:

α1

(R0 − R

)− (Id −K∗)λ = 0, a.e. x ∈ D, (2.25a)

α2

(Q0 − Q

)+

σK∗λ = 0, a.e. x ∈ D, (2.25b)

(Id −K) R(x) =(

c1 + K

(4π

σQ

)(x)

), a.e. x ∈ D. (2.25c)

Here, the operator K is defined in (2.11) and the constant c1 is given by (2.14).

A direct consequence is the following result.

Theorem 2 There exists a unique minimizer (R,Q) ∈ L2(D) of the optimization problem(2.3).

As seen in the calculations the formal adjoint equation to (1.5) are given by (2.23).

3 Solution Procedure

In this section, we present the numerical procedure used to solve the optimal controlproblem (2.3). We use a gradient method based on the formal state and adjoint equationsderived in the previous section. We discretize the governing equations in space and angulardirections. A different method is proposed by Kelley et.al. in [3]. A gradient methodapplied to the problem results in the following steps:

1. Given an initial control Q(x).

2. Loop until convergence:

(a) Compute solution to the state equation and obtain I(ω,x) by solving (1.5)

(b) Compute solution to the adjoint equation and obtain J(ω,x) by solving (2.4)

(c) Compute the gradient ∇QF by (2.5), i.e.,

∇QF(x) = α2

(Q(x)− Q(x)

)+

Sd

J(ω,x)dω (3.1)

9

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Table 3.1: Ordinates and weights used in the S8 discretization.

m µm ξm ηm wm

1 0.97097459 0.16912768 0.16912768 0.146138942 0.79878814 0.16912768 0.57735027 0.159838903 0.79878814 0.57735027 0.16912768 0.159838904 0.57735027 0.16912768 0.79878814 0.159838905 0.57735027 0.57735027 0.57735027 0.173346116 0.57735027 0.79878814 0.16912768 0.159838907 0.16912768 0.16912768 0.97097459 0.146138948 0.16912768 0.57735027 0.79878814 0.159838909 0.16912768 0.79878814 0.57735027 0.1598389010 0.16912768 0.97097459 0.16912768 0.14613894

(d) Choose a steplength δ such that the sufficient decrease condition [21] for F issatisfied and update the control by

Qnew(x) = Qold(x)− δ∇QF(x), ∀ x ∈ D. (3.2)

Note that, for the discrete problem, the control Q(x) has to be replaced by its discretevalues Qij at the gridpoints xij . An iteration in the step 2 requires the solution of theradiative transfer equation and its associated adjoint problem. The gradient in (3.1) isapproximate by a quotient difference whereas, the steplength δ is selected according tothe Armijo technique. Details on steepest descent methods can be found in standardtextbooks, see [21]. Other approaches to solve (2.3) are trust–region or SQP methods. Werefer to the literature for a detailed discussion, see [22, 2, 6].

3.1 Fully Discrete Problem

In the present work, the angle and space variables are discretized using a discrete ordinatesand finite volume method, respectively. For sake of brevity we shall formulate the methodsonly for the radiative transfer equation (1.5) and the adjoint equation (2.4) can be treatedin similar manner. The outstanding aspect of discrete ordinates method is that such anintegral is approximated by a low computational cost procedure, which is analogous tothe Gauss-Legendre method. It consists of the substitution of the integral term in (1.5)with a weighted summation of the integrand at selected ordinates of the unit sphere. Thismethod is sometimes referred to as the SN approximation, where N represents the numberof discrete values of direction cosines to be considered. In general, the total number ofordinate directions M in a set SN is given by M = N(N + 2)/2. The S8 discretizationis well designed for solving radiative transfer problem. For each direction ωm of thequadrature, a specific weight wm is associated with a set of three cosine angles µm, ξm

and ηm in the direct Cartesian grid (x, y, z). The cosine angles and the weights for S8

quadrature are listed in table 3.1. Other discrete SN sets can be found in [14, 5]. Forthe two-dimensional Cartesian coordinates, the radiative transfer equation (1.5) can beexpressed for each individual ordinate direction, m, as

µm∂Im∂x

+ ξm∂Im∂y

+ (σ + κ)Im =σ

M∑

k=1

wkIk + Q, m = 1, 2, . . . , M, (3.3)

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where Im denotes the radiant intensity at the discrete ordinate ωm. Next, the finitevolume technique is applied, which consists of the integration of the SN -equation (3.3)over a control volume such that shown in Figure 3.1. The result is an equation relatingthe value of an arbitrary function ψ at the nodal point, ψi+ 1

2j+ 1

2, to the value at each

adjacent line ψij , ψi+1j , ψij+1 and ψi+1j+1. The fully discrete problem corresponding tothe equation (1.5) is written as

µmIm,i+1j − Im,ij

(∆x)i+ 12

+ ξmIm,ij+1 − Im,ij

(∆y)j+ 12

+(σi+ 1

2j+ 1

2+ κi+ 1

2j+ 1

2

)Im,i+ 1

2j+ 1

2=

σi+ 12j+ 1

2

M∑

k=1

wkIk,i+ 12j+ 1

2+ Qi+ 1

2j+ 1

2, (3.4)

where the cell averages of a function ψ are given by

ψi+1j =1

(∆y)i+ 12

∫ yj+1

yj

ψ(xi, y)dy,

ψij+1 =1

(∆x)j+ 12

∫ xi+1

xi

ψ(x, yj)dx, (3.5)

ψij =1

(∆x)i+ 12(∆y)j+ 1

2

∫ xi+1

xi

∫ yj+1

yj

ψ(x, y)dxdy,

The cell center and cell boundary function in the fluxes (3.5) are related to each otherby a selected interpolation scheme. Here, we use the diamond difference method whichconsists of approximating the function values at the cell centers by the average of theirvalues at the neighboring nodes. Thus, the function value of ψi+ 1

2j+ 1

2at the cell center is

simply approximated by a bilinear interpolation as

ψi+ 12j+ 1

2=

ψij + ψi+ij + ψij+1 + ψi+1j+1

4. (3.6)

x

y

xi+1

x

yj+1

y

i

j (i,j) (i+1,j)

(i,j+1) (i+1,j+1)

xi+

21

j+y21

21(i+ ,j+ )

21

Figure 3.1: Spatial mesh and typical control volume.

With the introduction of the above interpolation relations into (3.4), the resultingfully discrete equations can be solved by proceeding in the direction of photon travel

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on the spatial mesh, that is, sweeping away from the boundary conditions in the mesh.For problems involving scattering media or reflecting boundaries, the discrete ordinatesequations are coupled and therefore have to be solved iteratively.

In order to formulate the equations (3.4) in a compact linear algebra form, we firstdefine the matrix entries

dm,i+ 12j+ 1

2:=

|µm|2(∆x)i+ 1

2

+|ξm|

2(∆y)j+ 12

+σi+ 1

2j+ 1

2+ κi+ 1

2j+ 1

2

4,

em,i+ 12j+ 1

2:=

|µm|2(∆x)i+ 1

2

+−|ξm|

2(∆y)j+ 12

+σi+ 1

2j+ 1

2+ κi+ 1

2j+ 1

2

4,

e¯l,i+ 1

2j+ 1

2:=

−|µm|2(∆x)i+ 1

2

+|ξm|

2(∆y)j+ 12

+σi+ 1

2j+ 1

2+ κi+ 1

2j+ 1

2

4,

el,i+ 12j+ 1

2:=

−|µm|2(∆x)i+ 1

2

+−|ξm|

2(∆y)j+ 12

+σi+ 1

2j+ 1

2+ κi+ 1

2j+ 1

2

4.

Define the vectors

Ψm ≡

Ψm,0...

Ψl,Ny

∈ R(Nx+1)(Ny+1), with Ψm,j ≡

Im,0j...

Il,Nxj

∈ RNx+1,

Φ ≡

Φ 12...

ΦNy− 12

∈ RNxNy, with Φj− 1

2≡

φ 12j− 1

2...

φNx− 12j− 1

2

∈ RNx;

and Qm ≡

Qm, 12

...Qm,Ny− 1

2

∈ RNxNy, with Qm,j− 1

2≡

qm, 12j− 1

2...

qm,Nx− 12j− 1

2

∈ RNx.

Recall that the SN -direction set used for the discrete ordinates formulation (3.3) avoidthe zero component in a given direction ωl. So, only one of the four cases; µm < 0 andξm < 0, µm < 0 and ξm > 0, µm > 0 and ξm < 0, or µm > 0 and ξm > 0 can hold. Herewe define the matrices Hm and Σm for the case µm < 0 and ξm < 0. The other threecases can be derived similarly.

Hm ≡

Dm E¯m. . . . . .

Dm E¯m

Dm SS

∈ R(Nx+1)(Ny+1)×(Nx+1)(Ny+1),

with

Dm ≡

d e. . . . . .

d e1

∈ R(Nx+1)×(Ny+1),

E¯m ≡

e. . . . . .

e1

∈ R(Nx+1)×(Ny+1),

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and S ≡

1 1. . . . . .

1 11

∈ R(Nx+1)×(Ny+1).

Σm ≡

Σm, 12

. . .Σm,Ny− 1

2

0

∈ R(Nx+1)(Ny+1)×NxNy, with

Σm,j ≡

σi+1

2 j+12+κ

i+12 j+1

24

. . .σ

i+12 j+1

2+κ

i+12 j+1

24

0

∈ R(Nx+1)×Ny.

With these definitions, the equation (3.4) can be written in the unknowns Ψ and Φ as

H1 −Σ1

. . ....

HM −ΣM

−ω1S . . . −ωMS I

Ψ1

...

ΨM

Φ

=

Q1

...

QM

0

, (3.7)

where I is the Nx×Ny identity matrix and 0 is the Nx null vector. The usual techniqueto solve the equation (3.7), is to eliminate the angular flux Ψ1, . . . ,ΨM using the Gaussianelimination. Therefore the storage requirements is reduced and the resulting equation

(I− 1

M∑

k=1

wkSH−1k Σk

)Φ =

14π

M∑

k=1

wkSH−1k Qk, (3.8)

is solved for the scalar flux Φ, which does not depend on direction variables.

The source iteration method and synthetic-diffusion acceleration are among the mostpopular techniques used in computational radiative transfer. Most recently, a class of mul-tilevel iterative solvers have been developed and experimented in [18, 20, 19] for radiativetransfer in participating media. All the results given through the paper were obtainedwith the GMRES algorithm the linear system (3.8) to be solved for the mean intensity Ronly. For a detailed formulation of this algorithm in both two and three space dimensionswe refer the reader to [18, 20] and [19], respectively.

4 Computational Results

We present numerical results for two test examples on optimal control problems in twospace dimensions. The first example considers the radiant source as a control variable,while the mean intensity is taken as control variable in the second example. In all theresults shown in this section, the S8-discrete ordinates set is used for the angle discretiza-tion in radiative transfer equation and its associated adjoint problem. We use constantboundary data A = 0 for all test cases. For the optimization we start with the initial guessQ0(x) = 0 for all x ∈ D. Furthermore, the steplength δ in (3.2) is chosen accordingly tothe Armijo rule [21].

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4.1 Example 1 (Source Inversion)

The first test-case is a source inversion problem. The computational domain is D = [0, 1]×[0, 1] discretized in 81×81 control volumes. The scattering and absorption coefficients areσ = κ = 1.

We set the desired source Q to be the sum of three Gaussian centered at (1/4, 3/4), (1/4, 1/4)and (3/4, 1/4), respectively, i.e.,

Q(x, y) =1√2

3∑

i=1

e−(x−xi)

2+(y−yi)2

2 .

We solve the transport equation with source Q to obtain R. Then we consider the sourceinversion problem,

minα1

2

D

(R− R

)dx +

α2

2

DQ2dx. (4.1)

We stop the optimization if the relative difference in the functional is less than 10−6.Plots of the contour lines of R(x) and Q(x) after the optimization can be found in theFigures 4.1-4.4. We observe that the position and strength of the placed sources could beretained by solving the optimization problem (4.1). We present results for different valuesof α1 and α2. In the Figures 4.1-4.2 we have a ratio α1/α2 = 100. The descent algorithmtakes 18 gradient steps and an average of 4.16 functional evaluations per gradient step toreach the desired tolerance. The detailed history of the optimization is given in Table 4.1.The results of the Figures 4.3-4.4 are obtained for α1/α2 = 1000. Here the descent methodtakes 64 gradient steps with average of 3 functional evaluations per descent step. Hence thetotal number of functional evaluations doubles as soon as the problem loses its convexityproperties. The history is similar to Table 4.1 and omitted.

Figure 4.1: Corresponding radiative flux R for the control Q after optimization (left) andradiative flux R of the desired control Q (right). The weights are α1 = 103 and α2 = 10.

4.2 Example 2 (Edging)

We start with a given pattern R and ask for an energy distribution (source term) Q gener-ating R. For instance a laser beam might deploy the energy Q in the domain D to generatethe desired pattern. Again, we compute the location of the source Q by solving (4.1). We

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Figure 4.2: Sources Q obtained by solving the optimization problem (4.1) and originalsource Q. The weights are α1 = 103 and α2 = 10.

prescribe a star-shaped pattern R as indicated in Figure 4.5. Contour lines of the solu-tion to the optimization problem can be found in Figures 4.6-4.7. The parameters for thisproblem are σ = 100 and κ = 1. The grid is 81×81 and we compare different ratios α1/α2.The descent method always starts with Q0(x) = 0 in D. In Figure 4.6 we set α1/α2 = 10.It takes 30 gradient steps to reach the desired tolerance with an average of 3.1 functionalevaluations per each descent step. In Figure 4.7 we set α1/α2 = 1000. Now the descentmethod takes 48 steps with an average of 6.3 functional evaluations per gradient step.Again we observe that the total number of functional evaluations increases as soon as theproblem loses its convexity property. The optimal radiosity distribution shows in all casesthe same star-shape pattern as the desired state.

5 Conclusions

We have presented an analytical and numerical study on optimal control problems oftracking type for RTE. Based on the adjoint calculus we derived the first–order optimalitycondition and proved the existence of an unique optimal control. For the numerical studywe devised a steepest descent method and proposed an appropriate discretization for theminimization. Numerical experiments in two space dimensional for the source inversionproblem are presented for the first time. Further research will focus on the time dependentproblem and on radiative heat transfer, which yields a nonlinear coupling with a heatequation.

Acknowledgments

This work has been supported by the Kaiserslautern Excellence Cluster Dependable Adap-tive Systems and Mathematical Modelling and by the DFG via SFB 568 and project PI408/3-1.

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Figure 4.3: Corresponding radiative flux R for the control Q after optimization (left) andradiative flux R of the desired control Q (right). The weights are α1 = 103 and α2 = 1.

Figure 4.4: Sources Q obtained by solving the optimization problem (4.1) and originalsource Q. The weights are α1 = 103 and α2 = 1.

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# Iteration∫D Q2dx

∫D(R− R)2dx # Funct. eval.

1 0 1.3551e-003 52 3.7476e-005 4.9534e-004 43 3.7899e-005 3.5740e-004 54 6.0886e-005 2.4621e-004 35 8.8711e-005 2.0483e-004 56 1.0887e-004 1.3709e-004 47 1.1444e-004 1.2272e-004 48 1.3672e-004 1.1630e-004 59 1.3407e-004 9.6782e-005 310 1.6366e-004 8.8055e-005 511 1.6104e-004 7.3293e-005 312 1.8651e-004 6.9475e-005 513 1.8414e-004 5.7925e-005 314 2.0674e-004 5.6220e-005 515 2.0464e-004 4.7040e-005 316 2.2494e-004 4.6318e-005 517 2.2309e-004 3.8958e-005 318 2.4147e-004 3.8704e-005 5

Table 4.1: History of the optimization process. Iteration number versus residual andnumber of functional evaluations in the Armijo stepsize rule

Figure 4.5: Contour line of the desired pattern R.

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Figure 4.6: Contour lines of the optimal source distribution Q and the correspondingradiosity R. Weights applied are α1 = 102 and α2 = 10.

Figure 4.7: Contour lines of the optimal source distribution Q and the correspondingradiosity R. Weights applied are α1 = 103 and α2 = 1.

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References

[1] V. I. Agoshkov, C. Bardos, Optimal Control Approach in Inverse Radiative Heat Trans-fer Problems: The Problem of the Boundary Function, 5, ESAIM: Control Optimisa-tion and Calculus of Variations, pp. 259-278, (2000)

[2] J.F. Bonnans, J.C. Gilbert, C. Lemarechal, C.A. Sagastizabal, Numerical Optimization- Theoretical and Practical Aspects, Springer (2002).

[3] J. M. Banoczi, C. T. Kelley, A Fast Multilevel Algorithm for the Solution of NonlinearSystems of Conductive-Radiative Heat Transfer Equations in Two Space Dimensions,20, SIAM J. Sci. Comp., pp. 1214–1228, (1999)

[4] M. K. Choudhary and N. T. Huff. Mathematical modeling in the glass industry: Anoverview of status and needs. Glastech. Ber. Glass Sci. Technol., 70:363–370, 1997.

[5] W. Fiveland, Discrete-Ordinates Solutions of the Radiative Transport Equation forRectangular Enclosures, J. Heat Transfer, 106, pp 699-706, 1984

[6] A. R. Conn, N. I. M. Gould, P. L. Toint, Trust-Region Methods, MPS/SIAM Series onOptimization, SIAM Philadelphia (2000)

[7] M. T. Laitinen and T. Tiihonen, Integro-differential equation modelling heat trans-fer in conduction, radiating and semitransparent materials, Mathematical Methods inApplied Sciences, 21, pp 375, 1998

[8] C. T. Kelley, Existence and uniqueness of solutions of nonlinear systems of conductive-radiative heat transfer equations, Trans. Theory and Statistical Physics, 25, pp. 249–260, (1996)

[9] E.W. Larsen, G. Thommes, A. Klar, M. Seaıd, and T. Gotz. Simplified Pn approxima-tions to the equations of radiative heat transfer in glass. J. Comp. Phys., 183:652–675,2002.

[10] D. Levermore. Moment closure hirarchies for kinetic theories. J. Stat. Phys., 83,1996.

[11] D. G. Luenberger, Optimization by Vector Space Methods., John Wiley & Sons, NewYork, 1969

[12] S. Manservisi, K. Heusermann, On some optimal control problems for the heat radia-tive transfer equation, 5, ESAIM: Control, Optimisation and Calculus of Variations,pp 425-444, (2000)

[13] D.Mihalas and B. S.Mihalas, Foundations of Radiation Hydrodynamics. Oxford Uni-versity Press, New York, 1983.

[14] M.F. Modest, Radiative Heat Transfer. McGraw-Hill, 1993.

[15] S.S. Pereverzyev, R. Pinnau and N. Siedow. Initial temperature reconstruction fora nonlinear heat equation: application to radiative and conductive heat transfer. D.Lesnic (ed.), Proceedings of the 5th International Conference on Inverse Problems inEngineering: Theory and Practice, Cambridge. Leeds University Press 2005. Vol. III,ch. P02, pp.1-8.

[16] R. Pinnau, A. Schulze. Newton’s Method for Optimal Temperature-Tracking of GlassCooling Processes. Submitted for publication, 2004.

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[17] R. Pinnau and G. Thommes. Optimal boundary control of glass cooling processes.M2AS, 120:1261, 2004.

[18] M. Seaıd and A. Klar, Efficient Preconditioning of Linear Systems Arising from theDiscretization of Radiative Transfer Equation, Lecture Notes in Computational Scienceand Engineering, 35, pp 211-236, 2003

[19] M. Seaıd, M. Frank, A. Klar, R. Pinnau and G. Thommes, Efficient Numerical Meth-ods for Radiation in Gas Turbines, J. Comp. Applied Math., 170, pp 217-239, 2004

[20] M. Seaıd, A. Klar and R. Pinnau, Numerical Solvers for Radiation and Conductionin High Temperature Gas Flows, Flow, Turbulence and Combustion, 3, pp 413-432,2005

[21] P. Spellucci, Numerische Verfahren der nichtlinearen Optimierung, Birkhauser Ver-lag, Basel, (1993)

[22] P. Spellucci, Nonlinear (local) optimization - the state of the art, preprint, (2001)

[23] G. Thommes, R. Pinnau, M. Seaid, T. Gotz, and A. Klar. Numerical methods andoptimal control for glass cooling processes. TTSP, 31(4-6):513–529, 2002.

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