RADIATION MODELING FOR BIO-MEDICAL APPLICATIONS A THESIS SUBMITTED IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF Bachelor of Technology In Mechanical Engineering By SAMIR CHOUDHURY Department of Mechanical Engineering National Institute of Technology Rourkela, Orissa 2009 RADIATION MODELING FOR BIO-MEDICAL APPLICATIONS A THESIS SUBMITTED IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF Bachelor of Technology In Mechanical Engineering By SAMIR CHOUDHURY Under the Guidance of Prof. S. K. Mahapatra Department of Mechanical Engineering National Institute of Technology Rourkela, Orissa 2009 National Institute of Technology Rourkela CERTIFICATE This is to certify that the thesis entitled, “RADATION MODELING FOR BIO-MEDICAL APPLICATIONS” submitted by Sri Samir Choudhury in partial fulfillment of the requirements for the award of Bachelor of Technology Degree in Mechanical Engineering at the National Institute of Technology, Rourkela (Deemed University) is an authentic work carried out by him under my supervision and guidance. To the best of my knowledge, the matter embodied in the thesis has not been submitted to any other University / Institute for the award of any Degree. Date:………………… Prof. S. K. Mahapatra Mechanical Engineering NIT ROURKELA ACKNOWLEDGEMENT The satisfaction and euphoria on the successful completion of any task would be incomplete without the mention of the people who made it possible whose constant guidance an encouragement crowned out effort with success. I am grateful to the Dept. of Mechanical Engineering, NIT ROURKELA, for giving me the opportunity to execute this project, which is an integral part of the curriculum in B.Tech programme at the National Institute of Technology, Rourkela. I would also like to take this opportunity to express heartfelt gratitude for my project guide Prof. S.K. Mahapatra, who provided me with valuable inputs at the critical stages of this project execution. I would like to acknowledge the support of every individual who assisted me in making this project a success and I would like to thank Mr. B. N. Padhi (a research scholar), for his help whenever it was required. Date:……………. SAMIR CHOUDHURY B.Tech (10503066) Dept. of Mechanical Engg. CONTENTS 1. ABSTRACT……………………………………………………………………….........i 2. LIST OF FIGURES…………………………………………………………………….ii 3. INTRODUCTION……………………………………………………………………...1 4. EQUATION OF RADIATIVE HEAT TRANSFER IN PARTICIPATING MEDIUM…………………………………………………………………………….........5 4.1 Absorption 4.2 Out-scattering 4.3 Emission 4.4 In-scattering 5. OVERALL ENERGY CONSERVATION EQUATION………………………………8 6. FINITE VOLUME METHOD…………………………………………………….........9 7. FORMULATION OF THE DISCRETIZATION EQUATIONS 7.1 Steady state RTE…………………………………………………………………..10 7.2 Solution procedure………………………………………………………………...13 7.3 Transient state RTE………………………………………………………………..14 7.4 Solution procedure………………………………………………………………...16 7.5 Linear anisotropic phase function…………………………………………………17 8. RESULTS AND DISCUSSIONS……………………………………………………..19 9. CONCLUSION………………………………………………………………………..35 10. FUTURE SCOPE OF RESEARCH……………………………………………........36 11. REFERENCES…………………………………………………………………........37 ABSTRACT Thermal radiation is important in many applications, and its analysis is difficult in the presence of a participating medium. In traditional engineering studies, the transient term of the radiative transfer equation (RTE) can be neglected. The assumption does not lead to important errors since the temporal variations of the observables e.g. temperature are slow as compared to the time of light of a photon. However in many new applications in different fields the transient effect must be considered in the RTE, like it has a great usability in the field of Bio-medical (applications like optical tomography, detection of scar tissues and many more all of which is interaction of LASER with the participating medium, tissue). In the transient phase, the reflected and the transmitted signals have temporal signatures that persist for a time period greater than the duration of the source pulse. This could be a source of information about the properties inside the medium. Hence sufficiently accurate solution methods are required. In the last few years, the finite volume method (FVM) and discrete transfer method has emerged as one of the most attractive methods for modeling steady and transient state radiative transfer. The present research work deals with the analysis of steady and transient radiative transfer in two dimensional square enclosure using FVM and analysis of steady and transient RTE with one boundary subjected to single short pulse irradiation. i LIST OF FIGURES Fig. I….A typical control volume Fig. II….Control angle discretization in Finite Volume method Fig.III….Different orientation of angles in a discretized control angle Fig. IV….Step Scheme for a control volume Fig.1…. Variation of dimensionless heat flux at the bottom wall for absorbing and emitting square enclosure. Fig.2…. Variation of dimensionless heat flux at the bottom wall for purely scattering square enclosure. Fig.3…. Variation of dimensionless heat flux along centerline in y-direction for isotropic scattering. Fig.4…. Variation of dimensionless heat flux along centerline in y-direction for linear backward scattering. Fig.5….Variation of dimensionless heat flux along centerline in y-direction for linear forward scattering. Fig.(i)….Geometry subjected to normal collimated incidence Fig.(ii)….Transmittance and Reflectance of a square enclosure Fig.6….Variation of transmittance and reflectance with distance in x-direction Fig.7…. Variation of transmittance with distance in x-direction for different wall emissivity Fig.8…. Variation of reflectance with distance in x-direction for different wall emissivity Fig.9…. Variation of transmittance with distance in x-direction for different anisotropic factor Fig.10…. Variation of reflectance with distance in x-direction for different anisotropic factor Fig.11…. Variation of transmittance with distance in x-direction for different angle of incidence ii Fig.12…. Variation of reflectance with distance in x-direction for different angle of incidence Fig.(a)….2-D square enclosure subjected to pulsed collimated incidence Fig.(b)….Unit Step pulse used to irradiate the bottom wall Fig.13….Variation of transmittance with non-dimensional time Fig.14….Variation of reflectance with non-dimensional time Fig.15….Variation of transmittance with non-dimensional time for different optical thickness Fig.16….Variation of reflectance with non-dimensional time for different optical thickness Fig.17….Variation of transmittance with non-dimensional time for different pulsewidth Fig.18….Variation of reflectance with non-dimensional time for different pulse-width Fig.19….Variation of transmittance with non-dimensional time for different scattering albedo Fig.20….Variation of reflectance with non-dimensional time for different scattering albedo Fig.21….Variation of transmittance with non-dimensional time for different anisotropic factor Fig.22….Variation of reflectance with non-dimensional time for different anisotropic factor Fig.23….Variation of transmittance with non-dimensional time for different angle of incidence Fig.24….Variation of reflectance with non-dimensional time for different angle of incidence iii INTRODUCTION For the last few decades, there is an exponential growth in the research area of transient radiative heat transfer in participating media. Traditional analysis of radiation transfer neglects the transient effect of light propagation due to the large speed of light compared to the local time and length scales [2]. As the technology advanced and the short pulsed laser applications developed, the steady state assumption was no longer valid as the temporal width of the input pulse was similar to the order of Pico and Femto-seconds. Ultra-short pulsed lasers are used in a wide variety of applications such as thin film property measurements, micro-machining, removal of contamination particles, ablation of polymers, remote sensing of the atmosphere, combustion chambers and other environments which involve interaction of the laser beam with scattering and absorbing particles of different sizes [3]. Another interesting application of short-pulsed lasers is in optical tomography where their use can potentially provide physiological and morphological information about the interior of living tissues and organs in a non-intrusive manner. All these applications need models to predict transient radiation transport in participating media. In the past, various analytical studies and numerical models of transient radiative transfer have been reviewed by Mitra and Kumar [4]. The normal-mode-expansion technique is used in [1] to obtain a semianalytical solution for the angular distribution of radiation at any optical distance within a linearly anisotropic scattering, absorbing, emitting, non-isothermal, gray medium between two parallel reflecting boundaries. From the literature it is evident that many researchers adopted different methods to deal with the problem. The commonly used methods to solve the transient radiative transfer equation are the Monte Carlo method, the integral equation solution, the finite volume method (FVM), the radiation element method (REM), discrete transfer method (DTM) and the discrete ordinates method (DOM). The Monte Carlo method is used to simulate problems involving radiative heat transfer because of its simplicity, the ease by which it can be applied to arbitrary configurations and its ability to capture actual and often complex physical conditions [5]. The Monte Carlo technique has been used by Guo et al. [5] to simulate short-pulsed laser 1|Page transport in anisotropically scattering and absorbing media. The authors examined the effects of pulse width, medium properties, and the effects of Fresnel reflection on the transmissivity and reflectivity of the medium. However, the method has inherent statistical errors due to its stochastic nature [2]. It also demands a lot of computational time and computer memory as the histories of the photons have to be stored at every instant of time [5]. Thus, the Monte-Carlo method is ruled out in practical utilizations such as real-time clinical diagnostics where computational efficiency and accuracy are major concerns [6]. Guo and Maruyama [7] evaluated the isotropic law in three dimensional inhomogeneous and linear anisotropic scattering media. The discrete ordinates method has been used by various researchers to solve the transient radiative transfer equation (RTE). Sakami et al. [8] used the DOM to analyze the ultra-short light pulse propagation in an anisotropically scattering two dimensional medium. Mitra et al [9] used a P1 approximation to model transient radiative transfer in a rectangular enclosure. Hsu [10] considered the Monte Carlo simulations for transient radiative transfer process within the participating media inside the one-dimensional geometry with the multiple scattering and reflective boundaries. Various effects, including the scattering albedo, pulse shape and width, surface reflectivity and optical thickness, are examined and concluded that if the boundary surface is reflective, then the temporal spread is influenced by multiple reflections and partial transmissions at the surfaces. The backward or reverse Monte Carlo method was successfully applied by Lu and Hsu [11] to simulate transient radiative transport in a non-emitting, absorbing, and anisotropically scattering one-dimensional slab subjected to ultra-short light pulse irradiation. Wu and Coworkers [12] and Tan and Hsu [13] have used the integral equation formulation to solve the transient radiative transfer problem analytically. Tan and Hsu [13] used the integral equation formulation and the radiation element method by Guo and Kumar [14] to simulate radiative transport in the same problem with black boundaries exposed to diffuse or collimated irradiation. Y.Hasegawa, et al., [15] used Monte Carlo method to simulate the transient light transmission through the living tissue which was characterized by strong forward scattering phase function. Brewster and Yamada [16] later conducted the transient study 2|Page using the same MC algorithm used by Hasegawa, et al. They examined various effects i.e., albedo, optical thickness, anisotropic scattering, and the detector size, on the reflected and transmitted temporal signals. Finite volume methods developed by Chai et al., [17] to solve the steady-state RTE have also been employed to solve the transient RTE by Chai [18,19]. The finite volume technique is used with the step and curved line advection method (CLAM) [20] spatial discretization schemes to model transient radiative transfer in 1-D and 2-D geometries. The author found that the CLAM scheme captures the penetration depths of radiation more accurately than the step scheme for the same grid. Rath et al., [21] extended the DTM, to solve transient radiative transport problems in a one-dimensional planar absorbing and scattering medium, one boundary of which is subjected to a short-pulse laser and the other boundary is cold. Effects of optical thickness, scattering albedo, and anisotropy factor on transmittance and reflectance are analyzed. Sarma et al., [22] analyzed the radiative heat transfer problem in 1-D planar absorbing, emitting and anisotropically scattering gray medium in radiative equilibrium subjected to collimated radiation by the discrete transfer method. The Galerkin method is extended by T. Okutucu; Y. Yener [23] for the solution of the transient radiative transfer problem in a one-dimensional participating plane-parallel grey medium with a collimated short-pulse Gaussian irradiation on one of its boundaries. The transient transmittance and reflectance of the medium are evaluated for various optical thicknesses, scattering albedos and pulse durations. Muthukumaran and Mishra [24] used the finite volume method for solving transient radiative heat transfer problem in a planar participating medium subjected to a short-pulse diffuse or collimated radiation. For a train of pulses, effects of the extinction coefficient and the scattering albedo on transmittance and reflectance signals are studied. A finite element model, which is based on the discrete ordinates method and leastsquares variational principle, is developed by W.An et al., [25] to simulate the transient radiative transfer in absorbing and scattering media in one dimensional and twodimensional enclosure and W.An et al., [26] extended the same method to simulate shortpulse light radiative transfer in homogeneous and nonhomogeneous media. Their results indicated that the reflected signals can imply the break of optical properties profile and 3|Page their location. Most recently Yilmazer A, Kocar C [27] discussed the radiative transfer problem in plane-parallel, participating medium with linearly anisotropic scattering using the ultraspherical-polynomials approximation method. Effects of the order of approximation, optical thickness, specular reflection, anisotropic scattering, and change of the source term on results are investigated different order of approximation. Majority of the findings are based on the most simplified assumption of black wall, whereas the reflective wall assumption resembles more to the practical application [4]. The multiple scattering and reflective boundaries, influences considerably the radiation transport in a participating medium. When the boundary surface becomes reflective, then the temporal spread changes significantly by the multiple reflections and partial transmissions at the surfaces [10]. Therefore, the present article focuses on the problem of a participating medium bounded by diffusely emitting boundaries, under the condition of radiative equilibrium. The total intensity is directly solved using FVM without splitting into the collimated part and diffusive part as cited in existing formulation [21, 22, 24, 28]. 4|Page EQUATION OF RADIATIVE HEAT TRANSFER IN A PARTICIPATING MEDIUM When the medium through which the radiative energy is traveling is participating then any incident beam will undergo Absorption Scattering Emission Scattering away from the direction under consideration is known as out-scattering and scattering from the other directions into the direction under consideration is known as inscattering. Absorption: The absolute amount of absorption is directly proportional to the magnitude of incident energy as well as the distance the beam travels through the medium. I k (r ) I (r , sˆ, t ) ds where k(r) is the linear absorption coefficient Out-scattering: It is same as absorption but only difference is that absorbed energy is converted into internal energy while scattered energy is simply redirected along another direction. I s (r ) I (r , sˆ, t ) s where s (r ) is known as the linear scattering coefficient 5|Page Emission: The rate of emission from a volume element is proportional to the magnitude of the volume. So the emitted intensity is proportional to the length of the path and local energy content in the medium. At the thermodynamic equilibrium intensity everywhere will be equal to blackbody intensity. I k (r ) I b s where k(r) is the emission constant same as for absorption In-scattering: It has contribution from all the directions and hence must be calculated by integration over all solid angles, considering the radiative heat flux impinging on a volume element from an infinitesimal pencil of rays in a specified direction. Scattering phase function: The scattering phase function in the RTE describes how radiation energy is scattered by a participating medium. Scattering can be classified into two categories. These are isotropic and anisotropic scattering. Isotropic scattering indicates energy scattered equally into all direction whereas anisotropic scattering can be forward and backward scattering. Scattering phase function satisfies the following relation: (sˆ, sˆ)d 4 4 where sˆ is the direction from which intensity is scattered into a direction ŝ . 6|Page Hence finally we have that energy flux scattered into a direction from all incoming directions is: I s (r ) I (r , sˆ' , t ) (r , sˆ' , sˆ, t )d' s 4 4 Making an energy balance on the radiative energy traveling in the direction we have change in the intensity found by summing all contribution from emission, absorption, out-scattering and in-scattering I ( s ds, sˆ, t dt ) I ( s, sˆ, t ) k (r ) I (r , sˆ, t ) s (r ) I (r , sˆ, t ) k (r ) I b s (r ) I (r , sˆ' , t ) (r , sˆ' , sˆ, t )d' 4 4 Expanding the left side of the above equation using Taylor’s Series and truncating after the first term we would the following equation as 1 I (r , sˆ, t ) I (r , sˆ, t ) k (r ) I (r , sˆ, t ) s (r ) I (r , sˆ, t ) c t s (r ) k (r ) I b s I (r , sˆ' , t ) (r , sˆ' , sˆ, t )d' 4 4 The above equation is known as the Radiative Heat Transfer equation in a participating medium. 7|Page OVERALL ENERGY CONSERVATION EQUATION Thermal radiation is one of the modes of hest transfer and must compete with conduction and convection. So the temperature field depends on all the three modes of heat transfer. The general form of the energy equation is: U .q p.v Q' ' ' t where u = internal energy v =velocity vector p = radiation pressure tensor q = total heat flux vector Q''' = heat generated within the medium = dissipation function = density of the medium As the medium is radiatively participating through emission, absorption and scattering so the second and third effect is negligible. Assuming U=CvdT and Fourier’s law of conduction to hold q = qr + qc In the absence of the heat generation Cv where T .( kT ) .qr t = density of the medium Cv = specific heat K = thermal conductivity T = temperature qr = radiative heat flux 8|Page FINITE VOLUME METHOD The basic idea of the control volume formulation is dividing the calculation domain into a number of non-overlapping control volumes such that there is one control volume surrounding each grid point. The differential equation is integrated over each control volume. Piecewise profiles expressing the variation between the grid points are used to evaluate the required integrals. The result is the discretization equation for a group of grid points. The discretization equation obtained expresses the conservation principle for the finite control volume as the differential equation expresses it for an infinitesimal control volume. (Fig.I) There are four basic rules which should be kept in mind during the formulation of the discretization equations are: 1.Consistency at the control-volume faces 2.All coefficients must always be positive 3.Negative slope linearization of the source term 4.Sum of the neighbour coefficients equal to the coefficients of the grid point under focus. 9|Page FORMULATION OF DISCRETIZATION EQUATION STEADY STATE RTE: A scattering, absorbing and emitting medium in a square enclosure with black wall is considered for the analysis. Discretizing the computational domain in both spatially and angular direction, then integrating the RTE over a control volume dV and control angle d and neglecting the effect of transient term (Fig.II) (Fig.III) 10 | P a g e I (r , sˆ, t ) dVd l (r ) I (r , sˆ, t )dVd l S l dVd l l s v l v l v After applying divergence theorem on LHS and intensity is assumed constant within a control volume and a control angle the above equation can be written as 4 I il Ai i 1 sˆ.nˆ d l l ml , P I Pl S m , P V l l On further simplification, for a control volume and a control angle the equation becomes I V I I A D I S V l P l l l m, P P l e l m, P l w x l cx l I nl I sl Ay Dcy l Using Step spatial differencing scheme (which sets the downstream boundary intensities equal to the upstream nodal intensities) (Fig.IV) l l l IP I el I nl , I sl I Sl , I w IW 11 | P a g e The discretized equation can be written in the following form alp I lp aWl IWl aSl I Sl b where l aWl yDcx l aSl xDcy l l a lp xDcy yDcx ( ml ) p vl b ( S ml ) p vl l 2 2 sin d d 1 1 l Dcex l Dcny ( sˆ .nˆ x )d l ( sˆ .nˆ y )d l ml S ml l l 2 2 sin cos sin dd Dcwx Dcx l l 1 1 2 2 sin sin sin dd Dcsy Dcy l l 1 1 s (r ) ll l 4 s ( r ) M l ' l 'l l ' k (r ) I b I 4 l ' 1, l ' l 12 | P a g e SOLUTION PROCEDURE: Algorithm l l W l S l p a , a , a , b are calculated Calculate al I l al I l b I lp W W l S S a p l l Guess unknown I nb(i.e I S , I W ) Set the current intensities as guessed value I Pl I lp I lp' / I lp 10 6 If Yes Record I Pl If No Take Updated I l and nb I Pl 13 | P a g e TRANSIENT STATE RTE: A scattering, absorbing and emitting medium in a square enclosure with black wall is considered for the analysis. Discretizing the computational domain in both spatially and angular direction, then integrating the RTE over a control volume dV, control angle d and a small time interval taking into account the effect of transient term 1 I l I l l l l dtdvd dtdvd I S dtdvd m m l V t c t s l Vt l V t Applying divergence theorem to the 2nd term and the magnitude of intensity is assumed to be constant over the control volume and a control angle. Under these assumptions and using the fully implicit scheme the above equation can be written as 4 1 l I P I Pl 0 V l I il Ai t sˆ.nˆ d l ml , P I Pl S ml , P V l t c i 1 l where I Pl 0 I Pl and are the nodal intensities at the start and at the end of the time step respectively. On further simplification, for a control volume and a control angle the equation becomes 1 l l l I P I Pl 0 Vl I el I wl Ax Dcx t I nl I sl Ay Dcy t c ml , P I Pl Sml , P Vl t where ml s ll l 4 14 | P a g e l Sm k Ib s M l l l I l 4 l 1 l l l Dcx sˆ.nˆ x d l l l Dcy sˆ.nˆ y d l d After applying the STEP scheme the final discretized equation looks like this, l l V l V l l l l Dcy Ay I P Dcx Ax m, P V ct ct l0 I P l l Dcx Ax I Wl S ml , P V l Dcy Ay I Sl In case the radiation intensity leaving a surface that is not black (i.e. gray) emits and reflects energy diffusely, then the change in the boundary intensity would be as following: ˆ, t ( r ) I b ( r , t ) I r , s 1 (r ) I (r , sˆ, t ) sˆ.nˆ d ˆ. n ˆ0 s where the 1st term is emissivity and the 2nd term is the reflectance of the surface. 15 | P a g e SOLUTION PROCEDURE: The finite volume discretization results in a set of algebraic equations with the radiation intensities as the unknowns. An iterative method is used to solve the resulting set of algebraic equations within each time step. The solution process adopts a marching procedure to solve the set of equations. The algorithm for the solution procedure is as follows: 1.Start with a suitable intensity distribution for the entire domain. 2.Proceed to the next time step. 3.Set the initial or the most current nodal intensities as the guessed values. 4.Update the upstream boundary intensities. 5.Following the marching order, calculate the nodal intensities for all internal control volumes. 6.Calculate the radiation arriving and living the opposite walls. 7.Return to step 4 and repeat the calculation until convergence. 8.Stop when the desired time is reached or go to step 2 to advance to a new time step. 16 | P a g e Linear Anisotropic phase function: In the previously formulated discretized equations the participating medium was taken to be isotropically emitting, absorbing and scattering. But in reality it doesn’t happens. The participating medium has some anisotropicity involved in it. So in the following formulation the linear anisotropic condition is derived and used in the code to make it more accurate and precise to have a proper understanding of the behavior of the medium. As seen earlier the scattering phase function is obeying the following condition (sˆ, sˆ)d 4 4 In the finite volume method this is approximated as l l 'l l' ˆ ˆ ( s , s ) d l '1 4 where l 'l = average energy scattered from control angle l’ to the control angle l. The scattering phase function can be represented in the form of a series M ( sˆ, sˆ) 1 AmPm(sˆ, sˆ) m 1 For isotropic condition M=0 For linear anisotropic condition M=1 Hence for linear anisotropy with M=1 we have ( sˆ, sˆ) 1 A1P1( sˆ, sˆ) 1 A1( sˆ, sˆ) 17 | P a g e where Pm is the Legendre’s Polynomial sˆ = Sinθ’ (cosφ’ iˆ + sinφ’ ĵ) + cosθ’ k̂ ŝ = Sinθ’ (cosφ iˆ + sinφ ĵ) + cosθ k̂ So, ( sˆ, sˆ) 1 A1{sin ' sin cos( ' ) cos ' cos } Average scattering phase function can be evaluated by l 'l (ŝ, ŝ)dΩ d ' l ' Hence 2 2 l 'l 1 1 {1 a cos cos ' a sin sin ' cos( ' )}sin ' d ' d ' 18 | P a g e RESULTS AND DISCUSSIONS 1. Isothermal Absorbing-Emitting Medium The medium is maintained at a constant temperature T. The black, square enclosure is having cold walls at 0 Kelvin. The calculation domain is discretized into 20x20 uniform control volumes in the X and Y directions. Finer angular discretizations is used that of 2x12 control angles with uniform in and the and directions respectively. Present John Chai 1.1 1 q* 0.9 0.8 0.7 0.6 0 0.1 0.2 0.3 0.4 0.5 X Lx Ly 1, ka 10, q* q T 4 (Fig.1) The above figure shows dimensionless heat flux at the bottom wall which is in good agreement with the published results. 19 | P a g e 2. Purely scattering medium A square enclosure is considered with black walls and the medium scatters energy isotropically with the scattering albedo ( = /) as unity. The bottom wall is hot maintained at a temperature Th with the remaining walls maintained at 0 Kelvin. Lx Ly 1, s 1, q*** q (Th4 Tc4 ) (Fig.2) The above figure shows dimensionless heat flux at the bottom wall which is in good agreement with the published results. 20 | P a g e 3. Linear Anisotropically Scattering Medium A square enclosure is considered with black walls and the medium scatters energy anisotropically with the scattering albedo ( = /) as unity. The bottom wall is hot maintained at a temperature Th with the remaining walls maintained at 0 Kelvin. The phase functions are studied using 25x25 control volumes and 6x24 control angles. Lx Ly 1, s 1, a 0, q *** q (Th4 Tc4 ) (Fig.3) The above figure shows dimensionless heat flux at the centerline in y-direction which is in good agreement with the published results. The figure below shows dimensionless heat flux at the centerline in y-direction. It is in good agreement with the published results for backward scattering B2 series as both have same number of terms in its expansion. 21 | P a g e Lx Ly 1, s 1, a 1, q *** q (T Tc4 ) (Fig.4) Lx Ly 1, s 1, a 1, q *** q (T Tc4 ) (Fig.5) 4 h 4 h The above figure shows dimensionless heat flux at the centerline in y-direction. The F1 series has more number of terms than linear forward scattering hence they do not agree but the trend is same which assures the correctness of simulation. 22 | P a g e 4. Collimated Incidence The top wall of the black, square enclosure is subjected to a normal collimated incidence (as shown in figure). The other walls are maintained at 0 Kelvin and the medium scatters energy isotropically with a scattering albedo of unity. The domain is divided into 25 x 25 control volumes and 3 x 24 control angles in the and directions. Step scheme is used in the present problem. The control angles are adjusted to capture the collimated incidence. Reflectance Collimated beam Fig. (i) Square Enclosure with collimated irradiation Transmittance Fig. (ii) Reflectance & Transmittance for an enclosure with collimated beam 23 | P a g e Transmittance Reflectance Lx Ly 1, s 1, k 0, q** q qc (Fig.6) Variation of wall emissivity: ε=1 ε=0.8 ε=0.4 (Fig.7) 24 | P a g e ε=1 ε=0.8 ε=0.4 (Fig.8) Variation of anisotropic factor: a=1 a=0 a=-1 (Fig.9) 25 | P a g e a=-1 a=0 a=1 (Fig.10) Variation of angle of incidence: 𝜭=90° 𝜭=45° 𝜭=30° (Fig.11) 26 | P a g e 𝜭=90° 𝜭=45° 𝜭=30° (Fig.12) 27 | P a g e 5. Temporal variations of the optical signals The bottom wall of the black, square enclosure is subjected to a normal collimated incidence (as shown in figure). The other walls are maintained at 0 Kelvin and the medium scatters energy isotropically with a scattering albedo of unity. A unit step pulse * as shown of a non-dimensional pulse width t p (ct p ) 1 is used to irradiate the wall and the different flux variation with non-dimensional time t ( ct ) is observed. * Fig.(a) collimated irradiation at the bottom wall. Fig.(b) Time of arrival of the collimated square pulse at different locations. 28 | P a g e (Fig.13) (Fig.14) a 0, 1, (L) 1, t *p (ct p ) 1 29 | P a g e Variation of Optical thickness: =0.5 =1 =2 (Fig.15) =0.5 =1 =2 (Fig.16) a 0, 1, t *p 1 30 | P a g e Variation of pulse-width: tp*=1 tp*=3 tp*=2 (Fig.17) tp*=3 tp*=1 tp*=2 a 0, 1, 1 (Fig.18) 31 | P a g e Variation of scattering albedo: =1 =0.75 =0 =0.5 (Fig.19) =1 =0.75 =0.5 =0 a 0, 1, t 1 (Fig.20) * p 32 | P a g e Variation of the anisotropic factor: a=1 a=0 a=-1 (Fig.21) a=-1 a=0 a=1 (Fig.22) t *p 1, 1, 1 33 | P a g e Variation of angle of incidence: =90 =45 =30 (Fig.23) =30 =45 =90 (Fig.24) a 0, 1, 1, t *p 1 34 | P a g e CONCLUSION Finite volume method found to be a suitable method for the simulation of collimated incidence problem with Steady and Transient RTE. Transmitted flux decreases considerably with the increase in optical thickness whereas reflectance increases. Reflected flux increases with the pulse width (nearly twice) whereas there is not much considerable change in transmitted flux. In the fully scattering medium both transmitted flux and reflected flux increases and reach their maximum. Linear forward scattering has more transmittance and less reflectance than the isotropic condition and vice-versa for the linear backward scattering. Transmittance decreases with the increase in the collimated angle whereas the reverse happens in the case of reflectance. Present study helps us to create a database for the healthy tissues. By comparing with the available information from the experiments, it will help to indentify the turbid tissues (damaged) if present. 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