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Drying Behaviour of Unpeeled Cashew Kernels in Steam Assisted Cross Flow Dryer


Affiliations
1 Cashew Research, Puttur (Karnataka), India
2 AICRP on Post Harvest Technology Scheme, University of Agricultural Sciences (G.K.V.K.), Bengaluru (Karnataka), India
     

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The performance of the steam assisted cross flow dryer employed in Indian cashewnut processing industry for drying unpeeled cashew kernels was assessed in terms of drying rate in relation to peeling efficiency. The rate of removal of moisture from unpeeled cashew kernels significantly varied with the location inside the dryer. Cashew kernels placed in close proximity to heat exchanger showed faster diffusion of moisture than other locations inside the dryer. Moisture content of unpeeled cashew kernels was reduced to less than 3.0 per cent (d.b) in the beginning i.e. First 3 hr of drying and reached below 1.0 per cent (d.b) after 9 hr of drying from the initial moisture content of 7.0 per cent (d.b). Movement of humid air towards outlet provided at the top of the dryer and circulation of hot air from bottom to top are the due reasons for the variation in the moisture from the unpeeled cashew kernels inside the dryer. Significant difference was found in the peeling efficiency of unpeeled cashew kernel dried up to 9 hr. Practically, moisture content of unpeeled cashew kernels reduced to 1.0 per cent after 9 hr of drying ensured manual peeling process better and kernels dried for 3 or 6 hr period could not attain the required moisture level to ease manual peeling. Total energy required to operate steam assisted cross flow dryer was found to be 16.49 per cent lesser than existing type of dryers in Indian cashewnut processing sector.

Keywords

Drying, Moisture Content, Unpeeled Cashew Kernels.
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  • Balasubramanian, D. (2007). Optimization of processing parameters using farm level cashew nut processing. J. Agric. Engg. Today, 32 (2) : 35-41.
  • Kumar, P.P., Paramashivappa, R., Vithayathil, P.J. and Rao, A.S. (2002). Process for isolation of cardolfrom technical cashew (Anacardium occidentale L.) nut shell liquid. J. Agric. & Food Chem., 50: 4705-4708.
  • Mandal, R.C. (1992). Cashew production and processing technology; Agro Botanical Publishers; India.
  • Mujumdar, A.S. (2006). Some recent developments in drying technologies appropriate for postharvest processing. Internat. J. Postharvest Technol. & Innovation, 1(1) : 76-92.
  • Raghavan, G.S.V., Rennie, T.J., Sunjka, P.S., Orsat, V., Phaphuangwittayakul, W. and Terdtoon, P. (2005). Overview of new techniques for drying biological materials with emphasis on energy aspects. Brazilian J. Chemical Engg., 22(2) : 195-201.
  • Suzanne Nielsen, S. (2003). Food analysis laboratory manual; Kluwer Academic / Plenum; NEWYORK, USA.
  • DCCD Statistics (2010). Available on http://dacnet.nic.in/
  • cashewcocoa/stat.htm#stat

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  • Drying Behaviour of Unpeeled Cashew Kernels in Steam Assisted Cross Flow Dryer

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Authors

D. Balasubramanian
Cashew Research, Puttur (Karnataka), India
T. N. Sandeep
AICRP on Post Harvest Technology Scheme, University of Agricultural Sciences (G.K.V.K.), Bengaluru (Karnataka), India

Abstract


The performance of the steam assisted cross flow dryer employed in Indian cashewnut processing industry for drying unpeeled cashew kernels was assessed in terms of drying rate in relation to peeling efficiency. The rate of removal of moisture from unpeeled cashew kernels significantly varied with the location inside the dryer. Cashew kernels placed in close proximity to heat exchanger showed faster diffusion of moisture than other locations inside the dryer. Moisture content of unpeeled cashew kernels was reduced to less than 3.0 per cent (d.b) in the beginning i.e. First 3 hr of drying and reached below 1.0 per cent (d.b) after 9 hr of drying from the initial moisture content of 7.0 per cent (d.b). Movement of humid air towards outlet provided at the top of the dryer and circulation of hot air from bottom to top are the due reasons for the variation in the moisture from the unpeeled cashew kernels inside the dryer. Significant difference was found in the peeling efficiency of unpeeled cashew kernel dried up to 9 hr. Practically, moisture content of unpeeled cashew kernels reduced to 1.0 per cent after 9 hr of drying ensured manual peeling process better and kernels dried for 3 or 6 hr period could not attain the required moisture level to ease manual peeling. Total energy required to operate steam assisted cross flow dryer was found to be 16.49 per cent lesser than existing type of dryers in Indian cashewnut processing sector.

Keywords


Drying, Moisture Content, Unpeeled Cashew Kernels.

References