Skip to main content

Performance Study of an Inclined Bubbling Fluidized Bed Dryer During Cashew Nut Drying

  • Conference paper
  • First Online:
Innovations in Energy, Power and Thermal Engineering

Part of the book series: Lecture Notes in Mechanical Engineering ((LNME))

  • 218 Accesses

Abstract

Raw cashew nuts were dried in a bubbling fluidized bed dryer at ambient temperature (an average of 32 °C) with bed inclinations of 0°, 15° and 30° using perforated (18.85%) and semi-circular (50%) opening distributor plates. The superficial velocity ranged from 1.4 m/s to 3.2 m/s for batch sizes of 0.5, 1, 2 and 2 kg raw cashew nuts + 2 kg sand. Raw cashew nuts alone and cashew nuts mixed with sand were taken for finding different hydrodynamic behaviour and energy consumptions. Samples were collected at 0, 30, 60 and 90 min intervals for moisture content removal measurement with air velocity of 2.5 m/s. When fluidized alone, the highest fluidization height of raw cashew nuts was 0.31 m for 2 kg inventory but when mixed with sand it was found 0.48 m at 15° bed inclination with air velocity as 2.5 m/s in 50% opening distributor plate. Average moisture removal was found to be 14.097 and 16.422% in semi-circular and perforated distributor plates respectively.

This is a preview of subscription content, log in via an institution to check access.

Access this chapter

Chapter
USD 29.95
Price excludes VAT (USA)
  • Available as PDF
  • Read on any device
  • Instant download
  • Own it forever
eBook
USD 189.00
Price excludes VAT (USA)
  • Available as EPUB and PDF
  • Read on any device
  • Instant download
  • Own it forever
Softcover Book
USD 249.99
Price excludes VAT (USA)
  • Compact, lightweight edition
  • Dispatched in 3 to 5 business days
  • Free shipping worldwide - see info
Hardcover Book
USD 249.99
Price excludes VAT (USA)
  • Durable hardcover edition
  • Dispatched in 3 to 5 business days
  • Free shipping worldwide - see info

Tax calculation will be finalised at checkout

Purchases are for personal use only

Institutional subscriptions

References

  1. Mohod A, Jain S, Powar AG (2011) Cashew nut processing: sources of environmental pollution and standards. BIOINFO Environ Pollut 1(1):5–11

    Google Scholar 

  2. Hebbar UH, Ramesh MN (2005) Optimisation of processing conditions for infrared drying of cashew kernels with testa. J Sci Food Agric 85(5):865–871

    Article  Google Scholar 

  3. Jekayinfa SO, Bamgboye AI (2006) Estimating energy requirement in cashew (Anacardium occidentale L.) nut processing operations. Energy 31(8–9):1305–1320

    Google Scholar 

  4. Asiru WB, Raji AO, Igbeka JC, Elemo GN (2013) Mathematical modelling of thin layer dried cashew kernels. Niger Food J 31(2):106–112

    Article  Google Scholar 

  5. Thant P, Robi PS, Mahanta P (2016) Experimental investigation of cereal crop drying in an inclined bubbling fluidized bed. IIT Guwahati, Ph.D. Thesis

    Google Scholar 

  6. Soponronnarit S, Prachayawarakorn S (1994) Optimum strategy for fluidized bed paddy drying. Drying Technol 12(7):1667–1686

    Article  Google Scholar 

  7. Hussainov M, Kartushinsky A, Mulgi A, Rudi Ü (1996) Gas-solid flow with the slip velocity of particles in a horizontal channel. J Aerosol Sci 27(1):41–59

    Article  Google Scholar 

  8. Yang H, Gautam M, Mei JS (1994) Gas velocity distribution in a circular circulating fluidized bed riser. Powder Technol 78(3):221–229

    Article  Google Scholar 

  9. Wang J, Shi Q, Huang Z, Gu Y, Musango L, Yang Y (2015) Experimental investigation of particle size effect on agglomeration behaviors in gas–solid fluidized beds. Ind Eng Chem Res 54(48):12177–12186

    Article  Google Scholar 

  10. Johari ANWAR, Taib MR (2007) Effect of sand sizes on the fluidization behavior in circular and rectangular columns. J Chem Natl Resour Eng 2:14–21

    Google Scholar 

  11. Neto P, Ribeiro AM, Pinho C (2012) Study on heat transfer from a bubbling fluidized bed combustor to a membrane wall. Int J Chem Reactor Eng 10(1)

    Google Scholar 

  12. Mahanta P, Patil RS, Pandey M (2010) Effect of particle size and sand inventory on wall-to-bed heat transfer characteristics of circulating fluidized bed riser. In Proceedings of the world congress on engineering 2010, vol II, WCE 2010, June 30–July2, London, U.K

    Google Scholar 

  13. Badday BA, Avssks G, Beddai AA, Naik MT (2014) Experimental study on the bed voidage and minimum fluidization velocity of gas-solid fluidization under different conditions. IPASJ Int J Mech Eng 2:22–26

    Google Scholar 

  14. Daud WRW (2008) Fluidized bed dryers-recent advances. Adv Powder Technol 19(5):403–418

    Article  Google Scholar 

  15. Chua KJ, Chou SK (2003) Low-cost drying methods for developing countries. Trends Food Sci Technol 14(12):519–528

    Article  Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Editor information

Editors and Affiliations

Rights and permissions

Reprints and permissions

Copyright information

© 2022 The Author(s), under exclusive license to Springer Nature Singapore Pte Ltd.

About this paper

Check for updates. Verify currency and authenticity via CrossMark

Cite this paper

Das, S., Mahanta, P., Sinha, A., Mishra, L. (2022). Performance Study of an Inclined Bubbling Fluidized Bed Dryer During Cashew Nut Drying. In: Palanisamy, M., Natarajan, S.K., Jayaraj, S., Sivalingam, M. (eds) Innovations in Energy, Power and Thermal Engineering . Lecture Notes in Mechanical Engineering. Springer, Singapore. https://doi.org/10.1007/978-981-16-4489-4_8

Download citation

  • DOI: https://doi.org/10.1007/978-981-16-4489-4_8

  • Published:

  • Publisher Name: Springer, Singapore

  • Print ISBN: 978-981-16-4488-7

  • Online ISBN: 978-981-16-4489-4

  • eBook Packages: EngineeringEngineering (R0)

Publish with us

Policies and ethics