Authors :
Onyekachi, C.P.; Obetta, S.E.; Igila, S.S.
Volume/Issue :
Volume 8 - 2023, Issue 11 - November
Google Scholar :
https://tinyurl.com/4j5ptbxt
Scribd :
https://tinyurl.com/y244mrxs
DOI :
https://doi.org/10.5281/zenodo.10171003
Abstract :
Development of a solar collector for drying
agricultural products, particularly vegetables, was
designed, constructed and evaluated. The primary
objective of the study was to tackle the issue prevalent in
many existing solar dryers, which are predominantly
stationary and consequently fail to optimize their power
output potential. Therefore, a solar tracking device was
formulated and constructed to trace the sun's trajectory,
ensuring the generation of the highest attainable power
and increase the energy harvested and thereby
optimizing the amount of energy received. The drying
apparatus primarily comprises a solar collector, a solar
tracking device, drying chamber and chimney The size
of the collector considered was 1219 mm x 609 mm,
comprising a single-layer glass with a thickness of 4 mm,
a black-painted aluminum absorber plate measuring 2
mm in thickness, and an insulation material with
thickness of 3 mm which was enclosed within a wooden
casing. The drying chamber was made of highly polished
wood frame and covered with plywood, consisting of
three drying trays. A 200–W wiper engine that swings a
collector configuration was adapted and this 200 watts
motor wiper makes it possible for the collector to attain
1500
rotation in a full wipe. Equipped with a sensor that
is calibrated to allow a track of 30 degrees in 120
minutes; in that way, optimum and down times are
appropriately captured. In assessing the various
conducted tests, the performance parameters considered
for evaluation comprised temperature, moisture content
of the produce, collector and drying efficiencies, drying
period, and drying rate. The moisture content of okra
experienced a reduction from 87 % (w.b,), 7.0 g H2O/g
solids(d.b) to 13% (w.b), 0.1 g H2O/g solids(d.b)
respectively and the moisture content of pepper
experienced a reduction from 83 % (w.b), 4.89 g H2O/g
solids(d.b) to 17 % (w.b), 0.03 g H2O/g solids (d.b)
respectively in a span of two to four days. The drying
rate for okra was identified to be 2.00 (g H2O/g solids)/h
whereas for pepper it was 0.67(g H2O/g solids)/h. The
collector efficiency was identified to be 25.24 % and
Drying efficiency was also identified to be 28.67%. The
drying curves, typical of thin layer type, produced
during the drying process, followed definite pattern
irrespective of the trays in the drying chamber. With the
polynomial behaviour, their equations, typical of Okra
was y = 0.3056x2
- 7.0526x + 43.633 and R2 were
estimated highly with correlation coefficient (R2
) ranging
from 91 to 99%, and for Pepper as: y = 0.61x2
- 10.166x
+ 46.168 and R2
values ranged from 83 – 94% - a
measure of theoretical correctness. These high values ofcorrelation coefficients obtained from the drying curves
bore reasonable closeness between the experiment and
theory. In all, these 2nd order equation models of these
curves, described the behaviour of the drying process.
This work provided a good insight into what possibilities
local technologies can do. The products of drying
displayed showed good indices of acceptability,
attainment of shelf-life moisture content, and showing
aesthetic and commercial appeals.
Development of a solar collector for drying
agricultural products, particularly vegetables, was
designed, constructed and evaluated. The primary
objective of the study was to tackle the issue prevalent in
many existing solar dryers, which are predominantly
stationary and consequently fail to optimize their power
output potential. Therefore, a solar tracking device was
formulated and constructed to trace the sun's trajectory,
ensuring the generation of the highest attainable power
and increase the energy harvested and thereby
optimizing the amount of energy received. The drying
apparatus primarily comprises a solar collector, a solar
tracking device, drying chamber and chimney The size
of the collector considered was 1219 mm x 609 mm,
comprising a single-layer glass with a thickness of 4 mm,
a black-painted aluminum absorber plate measuring 2
mm in thickness, and an insulation material with
thickness of 3 mm which was enclosed within a wooden
casing. The drying chamber was made of highly polished
wood frame and covered with plywood, consisting of
three drying trays. A 200–W wiper engine that swings a
collector configuration was adapted and this 200 watts
motor wiper makes it possible for the collector to attain
1500
rotation in a full wipe. Equipped with a sensor that
is calibrated to allow a track of 30 degrees in 120
minutes; in that way, optimum and down times are
appropriately captured. In assessing the various
conducted tests, the performance parameters considered
for evaluation comprised temperature, moisture content
of the produce, collector and drying efficiencies, drying
period, and drying rate. The moisture content of okra
experienced a reduction from 87 % (w.b,), 7.0 g H2O/g
solids(d.b) to 13% (w.b), 0.1 g H2O/g solids(d.b)
respectively and the moisture content of pepper
experienced a reduction from 83 % (w.b), 4.89 g H2O/g
solids(d.b) to 17 % (w.b), 0.03 g H2O/g solids (d.b)
respectively in a span of two to four days. The drying
rate for okra was identified to be 2.00 (g H2O/g solids)/h
whereas for pepper it was 0.67(g H2O/g solids)/h. The
collector efficiency was identified to be 25.24 % and
Drying efficiency was also identified to be 28.67%. The
drying curves, typical of thin layer type, produced
during the drying process, followed definite pattern
irrespective of the trays in the drying chamber. With the
polynomial behaviour, their equations, typical of Okra
was y = 0.3056x2
- 7.0526x + 43.633 and R2 were
estimated highly with correlation coefficient (R2
) ranging
from 91 to 99%, and for Pepper as: y = 0.61x2
- 10.166x
+ 46.168 and R2
values ranged from 83 – 94% - a
measure of theoretical correctness. These high values ofcorrelation coefficients obtained from the drying curves
bore reasonable closeness between the experiment and
theory. In all, these 2nd order equation models of these
curves, described the behaviour of the drying process.
This work provided a good insight into what possibilities
local technologies can do. The products of drying
displayed showed good indices of acceptability,
attainment of shelf-life moisture content, and showing
aesthetic and commercial appeals.