Abstract
Solar drying is one of the most important processes used by the farmers and the agriculture producers especially in developing countries, at the same time as using free solar energy permits to reduce the cost of the operation. However, in order to face or to limit the intermittent character of solar energy, storage is proposed as a solution. It is found that two ways are used for the thermal energy storage: thermal and chemical ways. Nevertheless, thermal way is the most useful for solar drying. We present, in this paper, a classification of the common methods of thermal energy storage applied to solar drying with the presentation of the optimum design parameters for the studied dryers. It was found that the most frequent materials used for energy storage during solar drying are packed-bed storage with the use of rocks, sands, or gravels. The packed bed can be added to the drying chamber, to the solar collector, or both of them. Also, desiccants, such as a mixture of several chemical products or wheat, can find applications as storage material used for solar drying process. Water is the other proposed storage material; it is used according to its availability, cost, and some of its thermo-physical characteristics. Latent heat storage has found a little application for solar drying. In general manner and depending on the dried product, the insert of the thermal energy storage increases the efficiencies of the solar dryers and allows recovering the surplus of solar radiations during sunshine periods for a reuse during the off-sunshine periods. The study is ended by an economic analysis of some developed solar dryers.
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Abbreviations
- A :
-
Surface (m2)
- C or Cp:
-
Specific heat capacity (J kg−1 °C−1)
- D :
-
Diameter (m)
- G :
-
Air mass velocity through grain bed/rock bed (kg s−1 m−2)
- g :
-
Gravitational acceleration (m s−2)
- H :
-
Height (m)
- h or h c :
-
Convective heat transfer coefficient (W m−2 °C−1)
- h as :
-
Adiabatic saturation humidity of air entering the drying chamber (kg water kg−1 dry air)
- h i :
-
Absolute humidity of air entering the drying chamber (kg water kg−1 dry air)
- I :
-
Hourly average solar radiation on inclined surface (W m−2)
- L c or L g :
-
Latent heat of vaporisation (J kg−1)
- M or m :
-
Mass (kg)
- Mev:
-
Hourly moisture evaporation (kg h−1)
- mw :
-
Moisture evaporated in time (kg s−1)
- m a or \(\dot{m}_{a}\) :
-
Mass flow rate (kg s−1)
- P d :
-
Blower power (J)
- Q f :
-
Amount of heat energy consumed by the fan (J)
- Q h :
-
Amount of heat energy given by the heater (J)
- Q p :
-
Amount of heat energy consumed by the pump (J)
- T :
-
Temperature (°C)
- T fHS :
-
Final temperature of heat storage material (°C)
- T iHS :
-
Initial temperature of heat storage material (°C)
- T i :
-
Inlet air temperature (°C)
- T :
-
Time (s)
- U L :
-
Overall heat loss coefficient from chimney (W m−2 °C−1)
- W :
-
Air humidity (kg kg−1)
- X :
-
Dimension (m)
- Z :
-
Height above drying bed (m)
- ΔP :
-
Pressure drop (N m−2)
- ΔT :
-
Difference between ambient and component air temperature (°C)
- β:
-
Coefficient of thermal expansion (°C−1)
- ε:
-
Porosity or emissivity
- η:
-
Thermal efficiency
- ρ:
-
Density (kg/m3)
- a:
-
Air or ambient
- b:
-
Packed bed
- c:
-
Crop or collector
- ch:
-
Chamber
- d:
-
Day
- E0 :
-
Inlet exchange-storage unit
- E1 :
-
Outlet exchange-storage unit
- f:
-
Fluid in grain
- g:
-
Global
- i:
-
Number of side wall of dryer or the number of reflector or inlet
- n:
-
Night
- o:
-
Outlet
- R:
-
Rock
- p:
-
Absorber plate or pickup
- RB:
-
Rock bed
- s:
-
Storage material
- t:
-
Time
- th:
-
Thermal
- w:
-
Water
- 0:
-
Initial
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The author is grateful to the Belgian National Fund of Scientific Research (F.R.S.-F.N.R.S.) for his short-term Foreign Postdoctoral Fellow position.
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Bennamoun, L. Improving Solar Dryers’ Performances Using Design and Thermal Heat Storage. Food Eng Rev 5, 230–248 (2013). https://doi.org/10.1007/s12393-013-9073-4
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DOI: https://doi.org/10.1007/s12393-013-9073-4