Mathematical modeling of intermittent and convective drying of rice and coffee using the reaction engineering approach (REA)

In order to extend shelf life of rice and coffee, drying can be conducted to minimize water content so that chemical and biological changes can be retarded. Several models have been proposed to model drying of coffee and rice. For design of dryer and evaluation of dryer performance, the effective and physically meaningful drying model should be implemented. The reaction engineering approach (REA) is applied in this study to model convective drying of coffee as well as convective and intermittent drying of rice. The REA is a unique approach to model drying; the physics of drying is captured by the relative activation energy which can be generated only from one accurate drying experiment. The relative activation energy can be applied to other conditions of drying provided the same material and similar initial moisture content. Results indicate that the REA describes the convective and intermittent drying of rice and coffee very well.

[1]  Greg Schoenau,et al.  Simulation and optimization of energy systems for in-bin drying of canola grain (rapeseed) , 1995 .

[2]  Siaw Kiang Chou,et al.  Analytical study of cyclic temperature drying: effect on drying kinetics and product quality , 2002 .

[3]  A. Mujumdar,et al.  Intermittent drying of bioproducts--an overview. , 2003, Bioresource technology.

[4]  Arun S. Mujumdar,et al.  Advances in drying , 1980 .

[5]  A. Iguaz,et al.  Effect of high temperature intermittent drying and tempering on rough rice quality , 2007 .

[6]  J. F. Steffe,et al.  Diffusion coefficients for predicting rice drying behaviour , 1982 .

[7]  Xiao Dong Chen,et al.  A Three-Dimensional Numerical Study of the Gas/Particle Interactions in an Industrial-Scale Spray Dryer for Milk Powder Production , 2009 .

[8]  Teresa R. S. Brandão,et al.  Estimation of water diffusivity parameters on grape dynamic drying , 2010 .

[9]  J. R. Limaverde,et al.  Heat and mass transfer in coffee fruits drying , 2005 .

[10]  R. B. Keey,et al.  Drying of Loose and Particulate Materials , 1992 .

[11]  D. Seth,et al.  A Lumped Parameter Model for Effective Moisture Diffusivity in Air Drying of Foods , 2004 .

[12]  M. A. Salgado-Cervantes,et al.  Modeling heat and mass transfer during drying of green coffee beans using prolate spheroidal geometry , 2008 .

[13]  Xiao Dong Chen,et al.  Fingerprints of the Drying Behaviour of Particulate or Thin Layer Food Materials Established Using a Reaction Engineering Model , 1997 .

[14]  T. A. Howell,et al.  Relationship of moisture content gradients and glass transition temperatures to head rice yield during cross-flow drying , 2003 .

[15]  T. Kudra,et al.  Enthalpy-Driven Optimization of Intermittent Drying , 2007 .

[16]  Baoming Li,et al.  Grain intermittent drying characteristics analyzed by a simplified model , 2006 .

[17]  R. Eggers,et al.  Heat and mass transfer during the coffee drying process , 2010 .

[18]  A Discussion on a Generalized Correlation for Drying Rate Modeling , 2005 .

[19]  Y. B. Li,et al.  STUDY ON ROUGH RICE FISSURING DURING INTERMITTENT DRYING , 1998 .

[20]  G. Y. Abawi,et al.  Optimization of solar grain drying in a continuous flow dryer , 1987 .

[21]  Gabriela Clemente,et al.  Enthalpy-driven optimization of intermittent drying of Mangifera indica L. , 2009 .

[22]  Oktay Hacıhafızoğlu,et al.  Modelling of intermittent drying of thin layer rough rice , 2007 .

[23]  Oktay Hacıhafızoğlu,et al.  Mathematical modelling of drying of thin layer rough rice , 2008 .

[24]  K. S. Jayaraman,et al.  DEHYDRATION OF FRUITS AND VEGETABLES - RECENT DEVELOPMENTS IN PRINCIPLES AND TECHNIQUES , 1992 .

[25]  W. Jomaa,et al.  Moisture diffusivity and drying kinetic equation of convective drying of grapes , 2002 .

[26]  Xiao Dong Chen,et al.  Air drying of milk droplet under constant and time‐dependent conditions , 2005 .

[27]  Mustafa Özilgen,et al.  The reaction engineering approach to modelling drying of thin layer of pulped Kiwifruit flesh under conditions of small Biot numbers , 2001 .

[28]  Xiao Dong Chen,et al.  The reaction engineering approach to modelling the cream and whey protein concentrate droplet drying , 2007 .

[29]  Terry J. Siebenmorgen,et al.  The glass transition temperature concept in rice drying and tempering : Effect on milling quality , 2000 .

[30]  I. I. Ruiz-López,et al.  Analytical solution for food-drying kinetics considering shrinkage and variable diffusivity , 2007 .

[31]  Xd Chen,et al.  A new model for the drying of milk droplets for fast computation purposes , 1999 .

[32]  R. Dong,et al.  Moisture distribution in a rice kernel during tempering drying , 2009 .

[33]  Stefan J. Kowalski,et al.  Modeling of Kinetics in Stationary and Intermittent Drying , 2010 .

[34]  Leandro dos Santos Coelho,et al.  Apparent thermal diffusivity estimation of the banana during drying using inverse method , 2008 .

[35]  M. N. Ramesh Moisture transfer properties of cooked rice during drying , 2003 .

[36]  Xiao Dong Chen,et al.  The Basics of a Reaction Engineering Approach to Modeling Air-Drying of Small Droplets or Thin-Layer Materials , 2008 .

[37]  Arun S. Mujumdar,et al.  On the Intermittent Drying of an Agricultural Product , 2000 .

[38]  A. Mujumdar,et al.  INTERMITTENT DRYING OF CARROT IN A VIBRATED FLUID BED: EFFECT ON PRODUCT QUALITY , 1999 .

[39]  Z. Pakowski,et al.  The Comparison of Two Models of Convective Drying of Shrinking Materials Using Apple Tissue as an Example , 2007 .

[40]  A. Cihan,et al.  A liquid diffusion model for thin-layer drying of rough rice , 2008 .

[41]  I. C. Macedo,et al.  Grain drying in stationary bins with solar heated air , 1976 .

[42]  J. Maté,et al.  Modelling effective moisture difusivity of rough rice (Lido cultivar) at low drying temperatures , 2003 .

[43]  M. N. Ozisik,et al.  On solar grain drying , 1980 .

[44]  T. Abe,et al.  THIN LAYER SOLAR DRYING CHARACTERISTICS OF ROUGH RICE UNDER NATURAL CONVECTION , 2001 .

[45]  Xiao Dong Chen,et al.  Numerical Study of the Drying Process of Different Sized Particles in an Industrial-Scale Spray Dryer , 2009 .

[46]  J. C. Ho,et al.  Batch drying of banana pieces - effect of stepwise change in drying air temperature on drying kinetics and product colour , 2001 .

[47]  Xiao Dong Chen,et al.  A Model for Drying of an Aqueous Lactose Droplet Using the Reaction Engineering Approach , 2006 .

[48]  A. Cihan,et al.  Liquid diffusion model for intermittent drying of rough rice , 2001 .

[49]  Timothy A. G. Langrish,et al.  Choosing an appropriate drying model for intermittent and continuous drying of bananas , 2007 .

[50]  T. Siebenmorgen,et al.  Relationship of Kernel Moisture Content Gradients and Glass Transition Temperatures to Head Rice Yield , 2003 .

[51]  A. Pawłowski,et al.  Drying of Wet Materials in Intermittent Conditions , 2010 .

[52]  Wan Ramli Wan Daud,et al.  CFD Evaluation of Droplet Drying Models in a Spray Dryer Fitted with a Rotary Atomizer , 2008 .

[53]  Miguel Ángel García-Alvarado,et al.  Modeling and simulation of heat and mass transfer during drying of solids with hemispherical shell geometry , 2011, Comput. Chem. Eng..

[54]  J. C. Ho,et al.  A diffusion model for drying of a heat sensitive solid under multiple heat input modes. , 2005, Bioresource technology.

[55]  S. Kowalski,et al.  Convective Drying Enhanced with Microwave and Infrared Radiation , 2009 .

[56]  W. P. Silva,et al.  Determination of effective diffusivity and convective mass transfer coefficient for cylindrical solids via analytical solution and inverse method: Application to the drying of rough rice , 2010 .