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و ﮐﺸﺎورزی ﻋﻠﻮم ﻣﺠﻠﻪ ﻃﺒﯿﻌﯽ ﻣﻨﺎﺑﻊ ﺟﻠﺪ ﭼﻬﺎردﻫﻢ ﺷﻤﺎره، دوم، ﺧﺮداد ـ ﺗﯿﺮ1386 www.sid.ir www.magiran.com/jasnr ﺧﺸﮏ ﻓﺮآﯾﻨﺪ ﺑﺮرﺳﯽ ﺳﯿﺎل و ﺛﺎﺑﺖ ﺑﺴﺘﺮ ﺷﺮاﯾﻂ در ﺷﻠﺘﻮک ﮐﺮدن* ﺧﻮش ﻣﺤﻤﺪﻫﺎدی ﺗﻘﺎﺿﺎ1 ، ﺻﺎدﻗﯽ ﻣﺮﺗﻀﯽ2 و ﭼﺎﯾﺠﺎن اﻣﯿﺮی رﺿﺎ3 1 ﻣﺎﺷﯿﻦ ﻣﮑﺎﻧﯿﮏ ﮔﺮوه داﻧﺸﯿﺎر ﻣﺪرس، ﺗﺮﺑﯿﺖ داﻧﺸﮕﺎه ﮐﺸﺎورزی ﻫﺎی2 ﻣﺎﺷﯿﻦ ﻣﮑﺎﻧﯿﮏ ﮔﺮوه اﺳﺘﺎدﯾﺎر اﺻﻔﻬﺎن، ﺻﻨﻌﺘﯽ داﻧﺸﮕﺎه ﮐﺸﺎورزی ﻫﺎی3 اﺳﺘﺎدﯾﺎر ﻣﺎﺷﯿﻦ ﻣﮑﺎﻧﯿﮏ ﮔﺮوه داﻧﺸﮕﺎه ﮐﺸﺎورزی ﻫﺎی ﺳﯿﻨﺎ ﺑﻮﻋﻠﯽ ﻫﻤﺪان، درﯾﺎﻓﺖ ﺗﺎرﯾﺦ: 22 / 4 / 82 ﺗﺎرﯾ ؛ ﭘﺬﯾﺮش: 6 / 6 / 85 ﭼﮑﯿﺪه روش ﻣﯿــﺎن در ﺧﺸــﮏ ﺟﺪﯾــﺪ ﻫــﺎی اﺳــﺖ ﺑﺮﺧــﻮردار ﺧﺎﺻــﯽ اﻫﻤﯿــﺖ از ﺳــﯿﺎل ﺑﺴــﺘﺮ روش ﮐــﺮدن،. ﻣﻄﺎﻟﻌــﻪ اﯾــﻦ در ﺧﺸـﮏ ﻓﺮآﯾﻨـﺪ روش ﺑـﻪ ﺷـﻠﺘﻮک ﮐـﺮدن ﻫـﺎ ی ﺑﺴـﺘﺮ و ﺛﺎﺑـﺖ ﺳـﯿﺎل، ﺧﺸـﮏ ﻧـﺮخ ﺣﺮارﺗـﯽ، راﻧـﺪﻣﺎن ﻧﻈـﺮ از ﻣﯿـﺰان و ﺷـﺪن ﺗﺮک ﮔﺮﻓـﺖ ﻗـﺮار ﻣﻘﺎﯾﺴـﻪ ﻣﻮرد داﻧﻪ ﺧﻮردﮔﯽ. آزﻣـﺎﯾﺶ ﻫـﺎ ﺧﺸـﮏ دﺳـﺘﮕﺎه ﯾـﮏ ﮐﻤـﮏ ﺑـﻪ آزﻣﺎﯾﺸـﮕﺎﻫﯽ ﺳـﯿﺎل ﺑﺴـﺘﺮ ﮐـﻦ ﺻــﻮرت داﺷــﺖ، را ﺳــﯿﺎل و ﺛﺎﺑــﺖ ﺑﺴــﺘﺮ ﺷــﺮاﯾﻂ اﻋﻤــﺎل و ﻣﺤﻔﻈــﻪ ﺑــﻪ ورودی ﻫــﻮای دﺑــﯽ و دﻣــﺎ ﮐﻨﺘــﺮل ﻗﺎﺑﻠﯿــﺖ ﮐــﻪ ﭘﺬﯾﺮﻓﺖ. ﺧﺸﮏ اوﻟﯿـ رﻃﻮﺑـﺖ ﻣﯿﺰان از ﺷﻠﺘﻮک ﮐﺮدن7 / 17 درﺻـﺪ ﻧﻬـﺎﯾﯽ رﻃﻮﺑـﺖ ﺗـﺎ11 درﺻـﺪ ﺳـﻪ در ﺧﺸـﮏ ﭘﺎﯾـﮥ ﺑـﺮ ورودی ﻫـﻮای دﻣـﺎی40 ، 60 و80 ﺳـﺎﻧﺘﯽ درﺟـﻪ ﮔـﺮاد ﺷـﺪ اﻧﺠـﺎم. ﺛﺎﺑـﺖ، ﺑﺴـﺘﺮ ﺷـﺮاﯾﻂ در اﺳـﺘﻔﺎده ﻣـﻮرد ﻫـﻮای ﺳـﺮﻋﺖ ﺳﯿﺎل و ﺳﯿﺎل ﻧﯿﻤﻪ ﺑـﻪ ﮐﺎﻣـﻞ ﺗﺮﺗﯿـﺐ1 / 0 ، 1 / 1 و5 / 3 ﺑـﻮد ﺛﺎﻧﯿـﻪ ﺑـﺮ ﻣﺘـﺮ. ﺧﺸـﮏ ﺣﺮارﺗـﯽ راﻧـﺪﻣﺎن ﻧﺴـﺒﺖ ﺑـﻪ ﺗﻮﺟـﻪ ﺑـﺎ ﮐـﻦ ﮔﺮدﯾـﺪ ﻣﺤﺎﺳـﺒﻪ ﺷـﺪه، ﺻـﺮف ﺣﺮارﺗـﯽ اﻧـﺮژی ﺑـﻪ ﻣﺤﺼـﻮل رﻃﻮﺑـﺖ ﺗﺒﺨﯿـﺮ ﺟﻬـﺖ ﻻزم اﻧﺮژی. ﺑﯿﺸـﺘﺮﯾﻦ راﻧـﺪﻣﺎن ﻘـﺪار ﺣﺮارﺗﯽ84 / 22 درﺻـﺪ آن ﻣﻘـﺪار ﮐﻤﺘـﺮﯾﻦ و33 / 3 درﺻـﺪ ﺑـﻪ، دﻣـﺎی در ﺛﺎﺑـﺖ ﺑﺴـﺘﺮ ﺷـﺮاﯾﻂ ﺑـﻪ ﻣﺮﺑـﻮط ﺗﺮﺗﯿـﺐ80 درﺟـﻪ ﺳﺎﻧﺘﯽ ﮔﺮاد ﺳﯿﺎل و دﻣﺎی در ﮐﺎﻣﻞ40 ﺳﺎﻧﺘﯽ درﺟﻪ ﮔـﺮاد ﺑـﻮد. داﻧـﻪ ﺗـﺮک اﺻـﻠﯽ ﻋﺎﻣـﻞ ﺷـﺪ، ﺗﻌﯿـﯿﻦ ﺛﺎﺑـﺖ ﺑﺴـﺘﺮ ﺷـﺮاﯾﻂ ﻫـﺎ، ﮐﻪ ﺑﻄﻮری ﺷـﺪن ﺧﺸـﮏ زﻣﺎن ﺑﯿﺸﺘﺮﯾﻦ) 280 دﻗﯿﻘـﻪ( و داﻧـﻪ ﺗـﺮک ﻣﻘـﺪار ﺑﯿﺸـﺘﺮﯾﻦ) 78 درﺻـﺪ( و ﺣﺎﻟـﺖ اﯾـﻦ ﺑـﻪ ﻣﺮﺑـﻮط دﻣﺎی80 ﺳﺎﻧﺘﯽ درﺟﻪ ﮔـﺮاد اﻧـﺪازه ﺷـﺪ ﮔﯿـﺮی. ﺧﺸـﮏ زﻣـﺎن ﮐﻤﺘـﺮﯾﻦ ﺷـﺪن) 40 دﻗﯿﻘـﻪ( ﺗـﺮک ﻣﻘـﺪار ﮐﻤﺘـﺮﯾﻦ ﻫﻤﭽﻨـﯿﻦ و داﻧﻪ) 17 درﺻﺪ( ﺑﻪ ﺳﯿﺎل ﻧﯿﻤﻪ ﺑﺴﺘﺮ ﺣﺎﻟﺖ ﺑﻪ ﻣﺮﺑﻮط ﻧﯿﺰ دﻣﺎﻫﺎی ﺑﺎ ﺗﺮﺗﯿﺐ80 و40 ﺳﺎﻧﺘﯽ درﺟﻪ ﮔﺮاد ﺑﻮد. واژه ﮐﻠﯿﺪی ﺎی: ﺧﺸﮏ ﻧﺮخ ﺣﺮارﺗﯽ، راﻧﺪﻣﺎن ﺳﯿﺎل، ﻧﯿﻤﻪ ﺷﻠﺘﻮک، ﺗﺮک ﺷﺪن، ﺧﻮردﮔﯽ ﻣﻘﺪﻣﻪ ﺧﺸـــﮏ ﻣﻬـــﻢ از ﯾﮑـــﯽ ﮐـــﺮدن روش ﺗـــﺮﯾﻦ ﻫـــﺎی دور ﮐــﻪ اﺳــﺖ ﮐﺸــﺎورزی ﻣﺤﺼــﻮﻻت ﻧﮕﻬــﺪاری ه ﻣــﯽ اﻓــﺰاﯾﺶ را ﻣﺤﺼــﻮﻻت اﯾــﻦ اﻧﺒــﺎرداری دﻫــﺪ. اﮐﺜــﺮ ﺧﺸــﮏ ﮐــﻦ ﻫــﻮای ﺟﺮﯾــﺎن از ﺻــﻨﻌﺘﯽ ﻫــﺎی داغ ﮐﺮدن ﺧﺸﮏ ﺟﻬﺖ ﻣﯽ اﺳﺘﻔﺎده ﮐﻨﻨﺪ. دﯾﮕﺮ، ﺳﻮی از ﺧﺸـــﮏ ﺟـــﺰء ﮐﺸـــﺎورزی ﻣﺤﺼـــﻮﻻت ﮐـــﺮدن ﻣــﯽ ﺷــﻤﺎر ﺑــﻪ ﻓﺮآﯾﻨــﺪﻫﺎﯾﯽ زﯾــﺎدی اﻧــﺮژی ﮐــﻪ رود ﻣـــﯽ ﻣﺼـــﺮف ﮐﻨـــﺪ. روش ﻣﯿـــﺎن در ﺟﺪﯾـــﺪ ﻫـــﺎی ﺧﺸـﮏ ﺧﺎﺻـﯽ اﻫﻤﯿـﺖ از ﺳـﯿﺎل ﺑﺴـﺘﺮ روش ﮐـﺮدن، اﺳﺖ ﺑﺮﺧﻮردار) ﭘﻬﻠﻮاﻧﺰاده،1377 .( ﺟﺮﯾﺎن ﻫﺮﮔﺎه* - ﻣﺴﺌﻮ ل ﻣﮑﺎﺗﺒﻪ: Khoshtag@ modares.ac.ir Archive of SID www.SID.ir

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    .37-48: 20 . . . 4.ASAE. 2000. ASAE Standard S352.2: Moisture measurment-unground grain and seeds. 47th edn.

    ST. Joseph. MI: U.S.A. 5.Di Mattia, D.G., Amyotte, P.R., and Hamdullahpur, F. 1996. Fluidized bed drying of large particles.

    Transactions of the ASAE. 39: 1745-1750. 6.Giner, S.A., and De Michelis, A. 1988. Evaluation of the thermal efficiency of wheat drying in

    fluidized bed: Influence of air temperature and heat recovery. Journal of Agricultural Engineering Research, 41: 11-23

    7.Kunii, D., and Levenspiel, O. 1991. Fluidization Engineering. Stoneham: Butterworth-Heinemann, U.S.A.

    8.McCabe, W.L., Smith, J.C., and Harriott, P. 1985. Unit operations of chemical engineering, 4th Edition. Singapore: McGraw-Hill Book Co.

    9.Prasad, B.V.S., Chandra, P.K., and Bal, S. 1994. Drying parboiled rough rice in stationary, semi-fluidized and fluidized conditions. Transactions of the ASAE, 37(2): 589-594.

    10.Rama Rao, V.V. 1974. Some studies on drying of parboiled paddy. Ph.D. thesis, Department of agricultural engineering, Indian Institute of Technology, Kharapur, India.

    11. Rawal, S.R. 1978. Studies on performance evaluation of heated air paddy driers. M. Tech. Diss., Department of agricultural engineering, Indian Institute of Technology, Kharapur, India.

    12.Schimdt, J.L., and Hukill, W.V. 1956. The effect of artificial drying on the yield of head rice and the germination of rice. Rice Journal, 59(13): 29-31.

    13.Sutherland, J.W., and Ghaly, T.F. 1990. Rapid fluid bed drying of paddy rice in the humid tropics. Proceeding of ASEAN Seminar on Postharvest Technology. Brunei Darussalam. 19-30.

    14.Treybal, R.E. 1980. Mass transfer operations, 3rd Edition. Tokyo: Mc Graw-Hill International Book Co.

    15.Uckan, G., and Ulku, S. 1986. Drying of grains in a batch fluidized bed dryer. In Drying of Solids- Recent International Developments, ed. A. S. Majumdar. New Dehli, India: Wiley Eastern Ltd.

    Archive of SID

    www.SID.ir

  • J. Agric. Sci. Natur. Resour., Vol. 14(2), June -July 2007 www.sid.ir

    www.magiran.com/jasnr

    Study of rough rice drying process in fixed and fluidized bed conditions

    M.H. Khoshtaghaza1, M. Sadeghi2 and R. Amirichayjan3

    1Associate Prof. of Agricultural machinery engineering Dept. of Tarbiat Modares University, 2Assistant Prof. of Farm machinery Dept., Isfahan University of Technology, 3Assistant Prof. Farm machiney Dept. Buali sina

    University

    Abstract

    Fluidized bed drying method is one of the most important new drying methods of agricultural materials. In this study the rough rice drying process by fixed and fluidized methods was compared based on thermal efficiency, drying rate and kernel fissuring percent. The experiments were conducted by a laboratory fluidized bed dryer with ability of the inlet air temperature and airflow rate control to operate in fixed and fluidized conditions. The rough rice samples were dried from 17.7 initial moisture content to 11% final moisture content (dry basis) at three temperatures of 40, 60 and 80C. The air velocity in fixed, semi-fluidized and fluidized bed conditions was 0.1, 1.1 and 3.5 m/s, respectively. The thermal efficiency of dryer was calculated based on the ratio of thermal energy utilized for evaporating water from the drying product to thermal energy supplied to the drying air. The maximum and minimum thermal efficiency of 22.84 and 3.3% were belonged to the fixed bed condition at 80C and the fluidized bed condition at 40C, respectively. The fixed bed condition was determined as the main factor influencing kernels fissuring, so that the maximum drying time of 280 minutes and the maximum kernel fissuring of 78% were measured in this condition at 80C. The minimum drying time of 40 minutes and the minimum kernel fissuring of 17% were belonged to the semi-fluidized bed condition at 80 and 40C, respectively. Keywords: Rough rice; Semi-fluidized; Thermal efficiency; Drying rate; Kernel fissuring

    Archive of SID

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