CFD Application on Food Industry; Energy Saving on the Bread Oven



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Iranica Journal of Energy & Environment 3 (3): 241-245, 2012 ISSN 2079-2115 IJEE an Official Peer Reviewed Journal of Babol Noshirvani University of Technology DOI: 10.5829/idosi.ijee.2012.03.03.0548 CFD Application on Food Industry; Energy Saving on the Bread Oven BUT 1 2 Ali Motamedzadegan and Shahla Khoddam 1 Sari Agricultural Science and Neutral Resources University, P.O. Box 578, Sari, Iran 2 Faculty of Food industry, Sari Agricultural Science and Neutral Resources University, Sari, Iran (Received: February 26, 2012; Accepted: May 28, 2012) Abstract: In this paper, application of computational fluid dynamics simulation of the cooking process of bread and energy saving inside an oven is presented. A two dimensional CFD model is applied to investigate the hot air distribution and bread cooking conditions inside the stove. Results are shown as velocity contours, turbulence intensity, static temperature and pressure distribution. It was found that the turbulence intensity was the highest at part of the stove, which means which part of bread would cook the fastest as it receives larger quantity of energy compared to other parts. The arrangement of the stove is discussed and some improvement offered to find a desire temperature distribution that leads to a suitable cooking process. In addition, the current results can be useful for next improvements on the existing stove for energy saving. Key words: CFD; Cooking Process; Air Flow Pattern; Numerical Method INTRODUCTION Hitesh et al. modeled 3-D CFD to simulate free convective heat flow in a thermal field coupled with radiative heat Computational fluid dynamics (CFD) is a simulation transfer inside an electric stove [10]. The aim of present tool which uses numerical methods and algorithms to was to investigate heat flow pattern in bread cooking solve and analyze problems associated with fluid flow [1]. oven. In addition more knowledge about air flow pattern CFD was originally developed from the pioneering through oven and more understanding about bread accomplishments of enthusiasts such as Richardson [2] condition cooking phenomena were obtained. This leads and Courant et al. [3], have obtained insight into fluid to design a new stove or to develop on existing ovens motion investigated the development of influential so that a high quality of food product is obtained [11]. numerical techniques [4]. Recent adoption of CFD has The purpose of the CFD simulation in this paper is to been implemented as a method of choice to investigate understand the air flow profile within the bread stove and the progression of the high costs and time consumption hence the heat distribution. associated with experimentation to produce an efficient method of choice of experiment. CFD is matured into a MATERIAL AND METHOD powerful tool in many industries such as food technology. The demonstration and powerfulness of General Governing Equations: The governing equations CFD are presented by number of researchers as cited of fluid flow and heat transfer can be considered as in ligatures [5-8]. In these studies, CFD was used as a mathematical model for the laws of conservation of fluid useful tool for calculation of the fluid flow, heat flow and often referred to as Naviere-Stokes equations. and mass transfer parameters [5, 7]. Furthermore, When these laws are applied to a fluid flow, these CFD has been used for modeling the processes involved conservation laws relate the rate of change of a desired in food processing and products especially in heating fluid property to external forces which are considered as stoves [4]. follows: Numerical and CFD methods have been used to simulate a bakery pilot oven in order to investigate three C The law of conservation of mass (continuity), which dimensional heat transfer mechanisms combined with the states the mass flows into a fluid element, exactly effects of turbulency introduced by Boulet et al. [9]. balanced with outlet mass flow [1]. Correspond Author: Shahla Khoddam, Sari Agricultural Science and Neutral Resources University, P.O. Box 578, Sari, Iran. E-mail: sh.khoddam@yahoo.com 241

ρ + ( ρui ) = 0 t x i (1) C The law of conservation of momentum (Newton s second law of motion), which states that the sum of the external forces acting on a fluid particle is equal to the rate of change of linear momentum. The momentum equation is stated as follows: u ( ) ( ) i u ρu i i + ρuiu j = pδ ij + µ + + ρgi t x j x j x j x i (2) Fig. 1: Geometrical overview of bread stove C The law of conservation of energy (the first law of thermodynamics), which states that the rate of Solution Procedure by CFD: In order to solve for a flow change of energy of a fluid particle is equal to heat field a general CFD code must take the mathematical transfer and the work done by the system (on statements inputted. The structured CFD model particles). The resulted equation is written as follows: incorporated into a suitable arrangement and solved for the specified boundary conditions [1]. Iterative methods T ( ρcat ) ( ρu jcat) + λ are commonly used by CFD codes to solve a whole set of = ST t x j x j x (3) discredited equations so that they can be applied to a j single dependent variable. Turbulence Equation: The present problem includes a fan Simulation Procedure which generates convective heat transfer as a dominated Geometry and Computational Domain: In any modeling heat sources. Cause of these circumstances and with procedure the first step is to define the primary physics attention to high speed of the fan, the flow regime of the modeling system. A physical model stands for through the oven assumed as turbulent. As the flow is the scientific features of a system which is modeled. turbulent, additional equations (standard K-ε model) for In current study, the two dimensional model is used turbulent viscosity are also solved [12]. to view the flow field from the side and above. The dimensions and location of the elements like fan, CFD Description and Implementation heating element and 4 breads are shown in Figure 1. Fluent Software: FLUENT Inc. offers three software The fan located on the wall for the goal of generating packages inside the CFD framework that are appropriate forced convection through the oven. for food engineer s modeling requirements [1]. The three packages are FLUENT (general purpose with Mesh Generation: Second step of the CFD analysis of metaphysics capabilities), FIDAP (modeling complex bread cooking model within a stove is designed for the physics) and POLYFLOW (polymer modeling). system geometry and its discretization into a FLUENT Inc. is presently one of the best leading computational grid of finite volumes. The mesh or grid suppliers of CFD software in the world. The most quality plays an important role in the accuracy and interesting features of the FLUENT software include stability of the CFD numerical computation [1]. For a 2D models for heat exchangers, discrete phase models for geometry, the mesh generator partitions the sub-domains multiphase flows, food industry such as ventilation, into triangular or quadrilateral mesh elements which drying, sterilization, refrigeration, cold display and storage contain nodes. If the boundary is curved (like the bread and mixing numerous high quality reaction models and the section area), these elements represent only an phase change model which tracks the melting and freezing approximation of the original geometry. Each of the points in the bulk fluid [1]. In this paper, the commercial element nodes has specific thermal properties of apparent CFD software Fluent (FLUENT Inc.) was used to simulate density, thermal conductivity, specific heat capacity, the flow field and heat transfer through the stove etc. The generated quadrilateral meshes are shown in including breads. Figure 2. 242

Fig. 2: Mesh Generation a) Whole Computational Domain and b) Enlargement of Bread s mesh Table 1: Boundary Conditions Fan Velocity 12 m/s (Normal to boundary) Total Heat Generation 1300 W/m 3 Initial Bread Temperature Ambient Wall Temperature Ambient Boundary Conditions: Boundary conditions are the physical assumptions that implement on the boundaries of the modeling cases. It means that CFD methods need these conditions to be solved. The relevant boundary conditions with respect to oven condition in the model are supplied depending on the required output of the model. Therefore, in present case, the boundary conditions are as following. The fan located at the top boundary of computational domain (Figure 1); that stands for the fan used in the real stove. This element is modeled as a velocity inlet source which means that air enters the oven from the top part. The heating elements are set constant at wall temperature together with the heat generation source. The rest of the domain are modeled as wall. The values of the boundary conditions are presented in Table 1. Fig. 3: Velocity Contours RESULTS AND DISCUSSIONS In this section results are presented in two categories. Flow field and thermal heat transfer are the important parts of cooking stove. The CFD investigation is stated as follows. Flow Field: The velocity contour and velocity vector of the whole stove domain are shown in Figures 3 and 4. The velocity of the hot air on the top of the bread cross section was higher than the bottom of the breads. Fig. 4: Velocity Vectors The velocity on the top was higher since the heat was contributed from both forced convection from the fan on one side and natural convection from the heating elements on the other sides. 243

Fig. 5: Contour of Static Pressure Fig. 7: Contour of Static Temperature Fig. 6: Contour of turbulent intensity Fig. 8: Contour of Enthalpy The contour of static pressure is shown in Figure 5. the stove. One of the options for setting a better mixing is It was observed that the high pressure is occurred at the that the displacement of the fan s stove. It is desired to top of two upon bread and at the bottom heating element. place the fan near by the heating element and thus the Figure 6 illustrates the result of turbulent intensity forced convection and natural convection make the better through the oven. Based on the turbulence results, large blend of heat transfer through the oven. amount energy is concentrated at the top of the bread and The results of the enthalpy calculation show similar the middle of the two bottom breads. In addition, trends of static temperature (Figure 8). presentation of results suggests that the sides of the bread which are facing the middle section of the bread CONCLUSION stove will be cooked fast; that was due to the high concentration of turbulence kinetic energy in this region. In this paper, a two-dimensional hot air flow CFD model within a bread stove is presented. The purpose of Heat Transfer: Contour of static temperature is shown in the CFD simulation is to determine the conditions through Figure 7. It was observed that the high temperature is the oven during the food preparation procedure in terms happened near by the heating elements at the left, right of heat distribution. The results showed that the CFD is and bottom sides. Because of the forced convection a reliable method for the investigation in food processing created by fan velocity, the heat from heating elements industries. In addition, the results showed that the air flow moves and rotates on the other sides of the oven. As a pattern inside the stove with the mentioned configuration consequence, the regions near the top breads catch the may not the best arrangements and it is possible the heat from the sources. Moreover, it can be seen that the flow pattern to be improved. One of the suggested temperature is not homogenous in the whole regions of procedure is change of the fan position inside the oven. 244

On the other hands the fan position can be changed and 6. Rafiee, S., A. Keyhani and A. Mohammadi, 2008. a desired temperature distribution obtained. In findings of Soybean Seeds Mass Transfer Simulation during the best fan position can be simulated by CFD model in Drying Using Finite Element Method, World Applied the future investigations. Sciences Journal, 4: 284-288. REFERENCES 7. Xia, B. and D.W. Sun, 2002. Applications of Computational Fluid Dynamics (CFD) In the Food Industry: A Review, Computers and Electronics in 1. Norton, T. and D.W. Sun, 2006. Computational fluid Agriculture, 34: 5-24. dynamics (CFD) e an effective and efficient design 8. Sebti, S.S., S.H. Khalilarya, I. Mirzaee, and analysis tool for the food industry: A review, S.F. Hosseinizadeh, S. Kashani and Trends in Food Science and Technology, 17: 600-620. M. Abdollahzadeh, 2011. A Numerical Investigation 2. Richardson, L.F., 1910. The approximate arithmetical of Solidification in Horizontal Concentric Annuli solution by finite differences of physical problems Filled with Nano-Enhanced Phase Change Material involving differential equations, with an application (NEPCM), World Applied Sciences Journal, 13: 09-15. to the stresses in a masonry dam, Philosophical 9. Boulet, M., M. Bernard, M. Dostie and C. Moresoli, Transactions of the Royal Society of London A, 2010. CFD Modeling of Heat Transfer and Flow Field 210: 307-357. in a Bakery Pilot Oven, Journal of Food Engineering, 3. Courant, R., K. Friedrichs and H. Lewy, 1928. Die 97: 393-402. partiellen differenzengleichungen der 10. Mistry, H., G. Subbu, S. Dey, P. Bishnori and mathematischen Physik, Mathematische Annalen J.L. Castillo, 2006. Modeling of Transient Natural (Historical Archive), 100: 32-74. Convection Heat Transfer in Electric Ovens, Applied 4. Shang, J.S., 2004. Three decades of accomplishments Thermal Engineering, 26: 2448-2456. in computational fluid dynamics, Progress in 11. Saxena, D.C., P. Haridas Rao and K.S.M. S Rao, 1995. Aerospace Sciences, 40: 173-197. Analysis of Modes of Heat Transfer in a Tandoor 5. Sajjadi, B., M.K. Moraveji and R. Davarnejad, Oven, Journal of Food Engineering, 26: 209-217. 2011. Investigation of Temperature and Influent 12. Mondal, A. and A.K. Datta, 2010. Two-dimensional Load on Nitrifying Treatment of Using Wastewater CFD modeling and simulation of crustless bread CFD, Iranica Journal of Energy and Environment, baking process, Journal of Food Engineering, 2: 08-17. 99: 166-174. 245