Numerical simulations and experimental measurements on the distribution of air and drying of round hay bales

The artificial drying of round bales offers the possibility to consistently produce quality hay by reducing field curing time and leaf shattering. Air distribution in the bale must be appropriate in order to achieve a uniform and efficient drying process. The air distribution and drying of four designs of round bale dryer were simulated using computational fluid dynamics. A round bale was modelled as a cylindrical porous media having a soft core. Bales were modelled both as being perfectly formed and as having a lower density close to their circular faces. Simulations showed that the simplest dryer design in which air enters the bale through one end, provides a deficient air distribution and inadequate drying, even when the bale is perfectly formed. Other designs studied showed, to varying degrees, an improved air distribution and drying uniformity. Simulations of a design in which an axial void is created in the bale centre, produced an optimal situation where the air and the drying front moves radially from the centre outwards. Conveying of air through both bale ends also contributed significantly to flow and drying uniformity. However, simulations for bales with a deficient density profile, as often found in practice, showed important distortions in the air distribution negatively affected drying. Therefore the uniformity of bale dry matter density is a determinant for the successful operation of any dryer. Additional efforts must be invested in the field to produce more uniform bales, particularly during raking and baling.

[1]  S. Phupaichitkun,et al.  CFD simulation of fixed bed dryer by using porous media concepts: Unpeeled longan case , 2013 .

[2]  A. Zomorodian,et al.  Applying CFD for designing a new fruit cabinet dryer , 2010 .

[3]  Thomas C. Bridges,et al.  Forced-Air Drying of Baled Alfalfa Hay , 1992 .

[4]  J. R. O'Callaghan,et al.  The effect of temperature on the drying rate of grass , 1971 .

[5]  P. V. Fonnesbeck,et al.  Estimating yield and nutrient losses due to rainfall on field-drying alfalfa hay , 1986 .

[6]  W. L. Kjelgaard,et al.  Air-Flow Resistance of Baled Alfalfa and Clover Hay , 1964 .

[7]  L. Tabil,et al.  Thermal conductivity and thermal diffusivity of timothy hay , 2006 .

[8]  Vassilis Belessiotis,et al.  Simulation of air movement in a dryer by computational fluid dynamics : Application for the drying of fruits , 1998 .

[9]  Pierre-Sylvain Mirade,et al.  Prediction of the air velocity field in modern meat dryers using unsteady computational fluid dynamics (CFD) models , 2003 .

[10]  S. Navarro,et al.  Evaluating aeration system efficiency. , 2002 .

[11]  Shahab Sokhansanj,et al.  Experimental Evaluation, Simulation and Optimization of a Commercial Heated-Air Batch Hay Drier: Part 1, Drier Functional Performance, Product Quality, and Economic Analysis of Drying , 1996 .

[12]  Dionissios P. Margaris,et al.  Dried product quality improvement by air flow manipulation in tray dryers , 2006 .

[13]  C. Rotz,et al.  A Model of Alfalfa Hay Storage , 1989 .

[14]  A. Williams The Permeability and Porosity of Grass Silage as Affected by Dry Matter , 1994 .

[15]  F. W. Bakker-Arkema,et al.  Drying and Storage Of Grains and Oilseeds , 1992 .

[16]  P. S. Mirade,et al.  A NUMERICAL STUDY OF THE AIRFLOW PATTERNS IN A SAUSAGE DRYER , 2000 .

[17]  Franz Román,et al.  Improvement of air distribution in a fixed-bed dryer using computational fluid dynamics , 2012 .

[18]  Graham R Thorpe,et al.  The application of computational fluid dynamics codes to simulate heat and moisture transfer in stored grains , 2008 .

[19]  Karl Kröll,et al.  Trockner und Trocknungsverfahren , 1959 .