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Related Concept Videos

Drying Shrinkage01:21

Drying Shrinkage

When hardened concrete is exposed to air with a relative humidity of less than 100 percent, it begins to lose the free water within its capillaries. As this water evaporates, the water initially adsorbed onto the calcium silicate hydrates migrates towards these now empty spaces and eventually evaporates as well. Over time, as more water leaves, the volume of the concrete decreases, a phenomenon known as drying shrinkage.
A portion of this drying shrinkage can be reversed; if the concrete is...

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Kinetics of potato drying using fluidized bed dryer.

Sushant Balasaheb Bakal1, Gyanendra Prasad Sharma, Somnath P Sonawane

  • 1Department of Processing and Food Engineering, CTAE, Maharana Pratap University of Agriculture and Technology, Udaipur, 313001 India.

Journal of Food Science and Technology
|October 2, 2013
PubMed
Summary

Potato drying kinetics were studied in a fluidized bed dryer, examining temperature and shape effects. The Page model accurately described moisture transfer, with temperature significantly impacting drying rates.

Keywords:
Activation energyAspect ratioCuboidal and cylindrical shapeDiffusivityFluidised bed dryingPotato

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Area of Science:

  • Food Science
  • Chemical Engineering
  • Materials Science

Background:

  • Fluidized bed drying is an efficient method for processing agricultural products like potatoes.
  • Understanding drying kinetics is crucial for optimizing process parameters and product quality.

Purpose of the Study:

  • To investigate the impact of air temperature and potato shape on drying kinetics.
  • To analyze moisture transfer using Fick's diffusion model and evaluate mathematical models for drying data.
  • To determine the activation energy for moisture diffusion.

Main Methods:

  • Potato samples (cuboidal and cylindrical shapes with varying aspect ratios) were dried in a fluidized bed dryer.
  • Drying experiments were conducted at air temperatures of 50, 60, and 70°C with an air velocity of 7 m/s.
  • Effective diffusivity was calculated, and the Page and simple exponential models were fitted to the experimental data.

Main Results:

  • Drying kinetics were significantly influenced by air temperature and potato geometry.
  • The Page model provided a better fit to the experimental drying data compared to the simple exponential model.
  • Arrhenius activation energy was determined, quantifying the temperature dependence of moisture diffusivity.

Conclusions:

  • Fluidized bed drying parameters, including temperature and sample shape, are critical for efficient potato drying.
  • The Page model is suitable for describing potato drying in a fluidized bed.
  • Temperature plays a key role in accelerating moisture diffusion during the drying process.