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Sunday, 25 December 2016
Performance of a solar-assisted solid desiccant dryer for oil palm fronds drying
Published Date
Solar Energy July 2016, Vol.132:415–429,doi:10.1016/j.solener.2016.03.041
Author
S. Misha a,b,,
S. Mat a
M.H. Ruslan a
E. Salleh a
K. Sopian a
aSolar Energy Research Institute, Universiti Kebangsaan Malaysia, 43600 Bangi, Selangor, Malaysia
bFaculty of Mechanical Engineering, Universiti Teknikal Malaysia Melaka, Hang Tuah Jaya, 76100 Durian Tunggal, Melaka, Malaysia
Received 11 March 2015. Revised 5 March 2016. Accepted 18 March 2016. Available online 2 April 2016. Communicated by: Associate Editor I. Farkas
Highlights
•
The use of desiccant material and solar energy produces good drying air condition.
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The solar energy contributes about 66% from the total energy used by the dryer.
•
The drying rate of oil palm fronds using dryer is higher than open sun drying.
•
The drying efficiency and pick up efficiency of solar dryer is high at full load.
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The developed solar dryer also can be utilized to dry any agricultural products.
Abstract A solar-assisted solid desiccant dryer was used to dry crushed oil palm fronds. Solar energy was used to heat water with a solar collector and heat was transferred to the air through two heat exchangers. The hot air is used for regeneration of desiccant wheel and increase temperature of drying air after dehumidification. Drying time for reducing the moisture content of crushed oil palm fronds from 69% to 29% under open sun drying was approximately 30 h and 40 min. Drying time was reduced by approximately 64%, 44%, and 33% for products in the first, second, and third columns of the developed solar dryer, respectively. Drying efficiency at full capacity was 19%, and 65% of the energy used was solar energy. Drying and pick-up efficiencies declined as the moisture content of the products decreased and less quantity of product in the drying chamber. The drying rate at full capacity was 8.37 kg/h, which is twice that of open sun drying (4.23 kg/h). Drying using semi-continuous mode was performed to reduce the drying time. The desiccant wheel contributed to improving drying air quality with sensible and latent effectiveness of 74% and 67%, respectively. The combination of desiccant and solar dryer produced better drying air condition, improved drying performance and consumed low electrical energy because solar energy was used as a primary energy source. Keywords
Solar dryer
Desiccant dryer
Oil palm fronds drying
Nomenclature
heat collection efficiency (%)
Qa
energy absorbed by the drying air (kW h or J) (mCpΔT)
Qc
solar radiation striking the collection area (kW h or J)
pick-up efficiency (%)
hi
absolute humidity of air entering the drying chamber (kg water/kg dry air)
ho
absolute humidity of air leaving the drying chamber (kg water/kg dry air)
has
absolute humidity of air entering the dryer at the point of adiabatic saturation (%)
W
weight of water evaporated from the product (kg)
density of air (kg/m3)
V
volumetric airflow rate (m3/s)
t
drying time (s)
L
latent heat of vaporization of water at exit air temperature (J/kg)
A
aperture area of the dryer (m2)
Pe
energy consumption of any electrical components (kW h or J)
I
hourly average solar radiation on the aperture surface (kW h/m2)
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