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Implementation of the first period of convective drying in a commercially available CFD package

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Języki publikacji
EN
Abstrakty
EN
The issue of the drying of woodchips is investigated in this paper. The most widespread type of the solid drying is a packed bed convective drying process with hot air as a working medium that is considered here. A comprehensive survey has proven a severe shortage of 3D drying-oriented computational fluid dynamics (CDF) packages for handling packed beds. This work was carried out by means of User Defined Procedures (UDF) – self written codes in C implemented in a commercially available CFD package – Ansys Fluent. A strongly flattened fixed bed of woodchips was investigated whose dimensions equaled to 1.5 m×1.5 m×0.2 m in length, width and height, respectively. In theoretical modeling woodchips were assumed as spheres of unique size settled in a cubic layout. The first period of drying was taken into consideration with the inlet air temperature 60 ◦C and humidity 0%. The temperature of the packed bed was set to the wet bulb temperature 21 ◦C. The vapor flux was implemented as a source term in the continuity equation. The core part of the UDF was a DEFINE_SOURCE macro that comprised the source term for evaporating water and partially the liquid water storage. As a result the drying air was humidified from initial 0%, to 22% along the bed, at a constant air enthalpy. The air temperature decreased from 60 ◦C to 38 ◦C, and the drying rate fell from 0.22 to 0.10 kg/m3s.
Słowa kluczowe
EN
Rocznik
Tom
Strony
139--157
Opis fizyczny
Bibliogr. 13 poz., rys., tab.
Twórcy
autor
  • Turbine Department, The Szewalski Institute of Fluid-Flow Machinery of the Polish Academy of Sciences, Fiszera 14, 80-231 Gdańsk, Poland
Bibliografia
  • [1] Gullman S.E.H.: Development of Evaporation Models for CFD. Goeteborg 2010.
  • [2] Jung C.-Y., Kim J.-R., Yi S.-C.: Two-dimensional simulation of silca gel drying using computational fluid dynamics. J. Ceram. Process. Res. 9(2008), 2, 184–188.
  • [3] Verdurmen R., Straatsma H., Verschueren M., Van Haren J., Smit E., Bargeman G., De Jong P.: Modelling spray drying processes for dairy products. http://lait.dairyjournal.org/articles/lait/pdf/2002/04/08.pdf.
  • [4] Getting Started Modeling Processes with Solids. Aspen Technology, Inc (February 2000).
  • [5] Jump Start: Modeling Convective Dryers in Aspen Plus V8.0. Available at: http://www.aspentech.com/Convective_Dryers_Plus.pdf.
  • [6] Andreasen M., Toftegaard R., Schneider P., Kaern M., Elmegaard B.: “Drypack” – a calculation and analysis tool. Available at: http://orbit.dtu.dk/fedora/objects/orbit:120943/datastreams/file_ a1193f86-9b77-4ff5- bc8f-dcd7b8be0f3c/content.
  • [7] Kudra T., Platon R., Navarri P.: Excel-Based Tool to Analyse Energy Performance of Convective Dryers. http://www.nrcan.gc.ca/sites/ www.nrcan.gc.ca/files/canmetenergy/files/ pubs/2009-003.pdf.
  • [8] Chourasia M., Goswani T.: CFD simulation of effects of operating parameters and product on heat transfer moisture loss in the stack of bagged potatoes. J. Food Eng. 80(2007), 947–960.
  • [9] Chourasia M., Goswani T.: Steady state CFD modeling of airflow, heat transfer and moisture loss in a commercial potato cold store. Int. J. Refrig. 30(2007), 672–689.
  • [10] Glover P.: Petrophysique. Département de Géologie et de Génie Géologique Université Laval.
  • [11] Seader J., Henley E., Roper D.: Separation Process Principles. Chemical and Biochemical Operations, 3rd Edn. Wiley & Sons, 2011.
  • [12] Ansys Fluent 12.0, UDF Manual, April 2009.
  • [13] Zhen-Xiang Gong, Arun S. Mujumdarb: Software for Design and Analysis of Drying Systems, Drying Technology: An Int. J. 26(2008), 7, 884-894, DOI: 10.1080/07373930802142390.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-3aef3d23-2146-42ec-83f2-e528358ab623
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