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Evaluation the effectiveness of an indirect solar dryer under Aswan governorate conditions

Authors:
Page 315 Hassan et al., 2023
`Vol. 4, No. 5, pp. 315-332, (December 2023)
DOI: 10.21608/aujes.2023.214979.1159
Aswan University Journal of Environmental Studies (AUJES)
Online ISSN: 2735-4237, Print ISSN: 2735-4229
Journal homepage: https://aujes.journals.ekb.eg/ E-mail: AUJES@aswu.edu.eg
Original research
Evaluation the effectiveness of an indirect solar dryer under Aswan
governorate conditions
Mostafa O. Hassan a *, Loai Nasrat b, Wael A. Mahmoud c and Taraby H.H.H.a
a Department of Agricultural Engineering and Biosystems, Faculty of Agriculture and Natural
Resources, Aswan University, Egypt.
b Electrical Engineering Department, Faculty of Engineering, Aswan University, Aswan,
Egypt.
c Faculty of Agricultural Engineering, Al-Azhar University (Assiut Branch), Assiut, Egypt.
Received: 4/6/2023 Accepted: 26/9/2023
© Unit of Environmental Studies and Development, Aswan University
Abstract:
This paper presents an evaluation of an indirect solar dryer consisting of a solar collector,
trays located in the drying chamber, and an air outlet opening above the drying chamber. The
solar collector consists of a Corrugated galvanized steel panel painted black and covered with
sheets of transparent glass, 3 mm thick from the top, and with dimensions of 2400 x 1100 mm.
The side walls of the solar collector are made of wood, are the insulation is thermal wool with a
50 mm thickness and are painted black from the outside. The drying room measures 1100 x 1200
mm, is made of wood, is thermally insulated from the inside, and contains a number of shelves.
The solar dryer was tested with a load of henna leaves, it was exposed to solar radiation from
8:00 a.m. to 3:00 p.m. A leaves of henna drying test is used to evaluate solar dryers, with a
maximum average temperature of 56.2 °C for the load test. 3000 g of henna leaves were used in
the load test to gauge how well the solar dryer worked. For the solar drying test, 3000 g of henna
leaves were dried from a starting moisture content of 74% W.b to a final moisture content of
8.4% in 7 hours of sunlight. The drying rate was calculated to be 306.7 g/h for the load test. The
drying efficiency was calculated to be 19.5%. The average collector efficiency was also
discovered to be 79.7% for the load test.
Keywords: Performance Evaluation, Drying, Solar Radiation, leaves of Henna.
1- Introduction
The biggest problem now facing humanity is energy. Nonrenewable and
renewable energy sources are the two main categories (Perlin, 1999). Energy research has
been rapidly progressing toward clean, sustainable, and renewable energy systems, such
wind, geothermal, and solar energy technologies, over the last few decades. These devices
were created for a number of uses, such as drying and heating (Chang and Kim, 2001;
Moummi et al., 2004; Battisti and Corrado, 2005).
_____________________________
Corresponding author*: E-mail address: mostafaomar@agr.aswu.edu.eg
Aswan University Journal of Environmental Studies (AUJES) 4 (5), pp. 315-332, (2023).
Online ISSN: 2735-4237, Print: ISSN 2735-4229. https://aujes.journals.ekb.eg/
Page 316 Hassan et al., 2023
Egypt's solar atlas, published in 1991, shows that it has a technical solar-thermal
electricity generating potential of 73.6 Peta watt hour, an annual direct normal energy
density of 19703200 kWh/m2, and 29003200 hours of sunshine (Comsan,2010).
Henna thrives in heavy, fertile clay soils that are completely drained. It thrives in
soils with a pH range of 4.3 to 8.0 and an annual precipitation of 0.2 to 4.2 meters. Henna
is exported in excess of 10,000 t annually. The top exporting nations are Pakistan, Iran,
Sudan, India, and Egypt, while the top importing nations are the Middle East and North
Africa, Western Europe, and North America. About 1000 t of henna herbs are exported
from Sudan annually. The United States (500-600 t/year), France (250 t/year), Saudi
Arabia (3000 t/year), and Great Britain (100 t/year) are the top four importers (Rehmat et
al.,2020).
Although it is generally agreed that properly designed forced-convection (active)
solar dryers are more selective and controllable than the natural-circulation (passive)
types, the latter are clearly inappropriate for remote rural village farm application in the
majority of developing countries due to the need for electricity or fossil-fuel driven fans
and/or the use of auxiliary heating sources, which makes both their capital, maintenance,
and operational costs prohibitive. The ''ventilated greenhouse dryer'' has the benefit of low
cost and simplicity in both on-site construction and operation for large scale applications
in rural areas (Ekechukwu and Norton,1999).
Drying is the process of removing moisture from a product, such as by lowering
water activity, which can slow down the rate of deterioration and retain the quality.
Agricultural products can be securely kept for several days if they are dried to eliminate
the maximum amount of moisture while retaining their active ingredients. Additionally,
the amount of free water in the meal is greatly reduced during this procedure, which
results in a concentration of dry matter without compromising the food's tissue,
wholesomeness, or outward appearance. This drying process involves the material's
internal mass and heat transfers (Lamidi et al., 2019).
The literature may show a variety of solar dryer kinds or designs. In light of the
ongoing advancements in solar dryer design, it should be developed to consistently update
the classifications of solar dryers. Additionally, other methods may be used to group solar
dryers. In fact, there are many different categories of solar dryers that have been
published in the literature (Chaudhari and Salve, 2014; Tiwari et al., 2016). In this
study, solar dryers are categorized based on the way air flows, how the sun heats the
product, and the type of drying chamber Figure (1.1) demonstrates the many types of
solar dryers.
Lawsonia inermis L., sometimes known as henna bushes, is a member of the
Lythraceae family of plants and is a shrub with both decorative and medicinal uses.
Henna is a perennial plant that may live for up to 10 years in the ground after being
planted. The stem, which contains colorful components, has simple, leathery leaves on
either side that become brown when the branches reach maturity. From the Babylonians
and the Pharaohs employed the henna plant in their religious rites, it is regarded as one of
the medicinal, aromatic, and cosmetic plants that man has known since the dawn of the
earliest civilizations. It is a tropical plant that presumably originated in South America,
Aswan University Journal of Environmental Studies (AUJES) 4 (5), pp. 315-332, (2023).
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Page 317 Hassan et al., 2023
Iran, or India. Cultivation of the plant has since expanded to Australia, North Africa, and
southwest Asia (Ghani et al., 2021).
Figure (1): Classifications of solar dryers
Drying requires a lot of energy to do. The use of conventional and fossil fuel heating is
expensive, inefficient for drying, and emits unwanted CO2.Since it causes erosion and
desertification, burning biomass is not a wise choice for heating. Drying typically involves the
use of expensive energy sources like electricity or a mix of solar energy and another type of
energy. Harnessing solar energy for heating agricultural goods is a low-cost solution in terms of
both capital and operating expenditures (Akuffo et al., 2003). Solar energy is abundant in these
remote areas of Egypt, where the amount of sunshine hours is around 3500 h/year (Ahmad and
Schmid, 2002).
2. Materials and Methods
The performance assessment test was conducted using an indirect solar dryer. The indirect
solar dryer was constructed in the workshop and tested on the campus of the College of
Agriculture and Natural Resources at Aswan University, Egypt.
2.1. Components of the solar dryer
An indirect solar dryer consisting of a solar collector (SC), trays located in the drying
chamber and exhaust fan.
2.1.1 Solar collector SC
The primary goal in building the solar collector was to use locally available materials to
collect as much solar energy as possible at the lowest possible cost. SC performance evaluations
were carried out in Egypt's governorate of Aswan. Latitude and longitude are 24.06° and 32.45°,
respectively, with 14 hours of daylight and I = 8.2 KWh/m2 per day for a 24.06° solar declination
angle. It is painted black to keep the heat inside and is thermally insulated with thermal wool that
has a thickness of 50 mm. Three main parts make up the solar collector: The glass cover is 2400
mm long, 1100 mm wide, and 3 mm thick. The cover is fastened to a 100 mm-thick wooden
frame. Corrugated galvanized steel black plate is used to create the absorber plate, the height
between them was 10 cm. Thermal wool with a 50 mm thickness serves as shown figure (2).
Aswan University Journal of Environmental Studies (AUJES) 4 (5), pp. 315-332, (2023).
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Page 318 Hassan et al., 2023
Figure(2): solar collector “SC”.
2.1.1.1. Solar collector absorber plate
The air fluid receives the collected energy through the energy absorber plate. For effective
heat absorption, the absorber plate was constructed from a Corrugated galvanized steel plate that
was one millimeter thick and black-coated. 50° is the rib angle, and 5 cm is the top height.
2.1.1.2. Transparent glass cover.
In order to increase the temperature of the absorbent surface, the transparent glass plate absorbs
the solar radiation that is directed towards it and allows it to enter the interior. The glass cover is
3 mm thick, 2400 mm long, and 1100 mm wide. Table (1) dimensions solar collector absorber
plate and transparent glass cover.
Table (1) dimensions solar collector absorber plate and transparent glass cover.
Properties of cover material glass
Solar spectrum refractive index:
1.52
Transmittance:
0.89
Number of covers:
1
Cover-plate air spacing:
150 mm
solar collector glass cover dimensions length
2400mm
SC width
1100 mm
SC absorber area
2.256m2
Properties of absorber plate
Conductivity Iron:
60.50 W/m k0
Thickness:
1 mm
Solar spectrum absorbance:
0.88
Aswan University Journal of Environmental Studies (AUJES) 4 (5), pp. 315-332, (2023).
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Page 319 Hassan et al., 2023
Properties of cover material glass
Long-wave emittance:
0.15
top height
50 mm
Ribbing angle
50o
solar collector absorber dimensions length
2400mm
SC width
940 mm
SC absorber area
2.256 mm
2.2. The drying chamber.
The drying chamber is made of wood with a thickness of 30 mm. It is thermally insulated
by thermal wool with a thickness of 5 cm and painted black to trap the heat inside. The
manufactured drying chamber can accommodate three or more trays and has an exhaust hole. The
drying chamber has a length of 1100 mm, width of 0.65 m and height of 1200 mm. It is equipped
with a two-piece door in the front. It is about 800 mm above the ground and carried on 4 legs.
2.3. Exhaust Fan/Ventilation Fan.
DC 12V exhaust fan, Material Plastic, with a diameter of 16 cm, a size of 150 mm, a
capacity of 20 watts, and a frequency of 50 Hz. It is installed inside a circular hole; axial fan was
used to draw hot air to the chamber Dryer.
Table (2) Ventilation Fan specifications
speed
Diameter
capacity
type
volt
Material
3
15 cm
20 watts
DC
12V
Plastic
2.4 Measuring instruments
2.4.1. Solar intensity device
System temperatures were recorded by the digital thermometer and the different measured
point of a prototype using thermocouple type K, Ranged from -200 to 1250 oC, with accuracy of
± 1%+3. A Pyranometer model PSP was used to measure the solar radiation sensitive to 9 µV per
W/m2. The Pyranometer readings were linear to ±0.5% in measurement ranged from 0 to 2800
W/m2.
2.4.2 Anemometer.
The anemometer apparatus is used for measuring air speed their specifications are shown in
Table (3). Table (3): Specifications of the anemometer.
Air Velocity
Range
Resolution
Accuracy
meters per sec
0 - 30m/s m/s
0. 1 m/s
± (3% + 0.20 m/s)
Air Flow
Range
Resolution
Area
cubic meters/min
0-9999 m3/min
1
0 to 9.999 m2
Air Temperature
Range
Resolution
Accuracy
10 - 50 Deg.C
0.1 oF/c
4.0 oF (2.0 oC)
Model UT363.
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Page 320 Hassan et al., 2023
24.3 Electronic balance.
Model DT2000, Capacity(g) 2000, Readability(mg) 0.5, Linearity error(g) ≤±1, Plan size
173x135mm, Dimension 230x178x66mm and Voltage AC 220V.The initial weight of the henna
leaves to be dried was determined with an electronic balance Sensitive scale with three decimal
digitsbefore being inserted in the dryer. The weight was determined at every one-hour interval
during the drying process.
2.4.4. Electronic circuit.
Table (4): Specifications of the Electronic circuit.
Q
Parameter
Specification
Job
Figures
1
Adriano Uno
(ATmega328)
Operating Voltage
5V. DC Current
for 3.3V Pin: 50
mA. Flash
Memory: 32 KB.
SRAM: 2
KB(ATmega328P)
Data storage
5
Precision
Digital
Temperature
and Humidity
Sensor
Module
(DHT22))
3 to 5V power and
I/O. 2.5mA max
current use during
conversion (while
requesting data).
Good for 0-100%
humidity readings
with 2-5%
accuracy.
Good for -40 to
25°C temperature
readings±0.5°C
accuracy.0.5Hz
sampling rate.
A digital
temperature
and humidity
sensor.
1
Digital
Temperature
Sensor
Module
(DS18B20)
Unique1-Wire
interface requires
only one port pin
for
communication.
Each device has a
unique 64-bit
serial code stored
in an onboard
ROM.
Can be powered
from data line.
Power supply
range is 3.0V to
provides 9-bit
to12-bit
temperature
measurements
and has an
alarm
function with
on volatile
user-
programmable
upper and
lower trigger
points.
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Page 321 Hassan et al., 2023
Q
Parameter
Specification
Job
Figures
5.5V.
Measures
temperatures from
55°C to +125°C.
Thermometer
resolution is user-
selectable from 9
to 12 bits.
User-definable
nonvolatile (NV)
alarm settings
with Alarm search
command.
identifies devices
whose temperature
is outside of
programmed
limits.
A device for measuring temperature and humidity is shown in the following figure (3):
Figure (3): The circuit diagram
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2.5. Performance evaluation of the solar dryer:
2.5.1 Solar collector efficiency
The solar collector was built on the presumption that it operates in a steady state, so the
system analysis techniques described here can be used to use the thermal performance analysis to
maximize system efficiency by Duffie and Beckman (1991); Kalogirou (2004); and ASHREA
(2005) as follows:

 ................................................................... 1
Where; I is the solar radiation flux incident on the tilted surface of the SC W/m2, Qu is the
useful energy gain per time a solar collector "W".
  󰇛󰇜 ....................................................... 2
where Qi is the absorbed solar energy, and A is the surface area of collector (m2), is the
transmittance of the SC covers, and is the absorptance of the SC plate.
Overall heat transfer coefficient (Awady, 1999).
󰇛 󰇜 ................................................. 3
󰇛󰇜-󰇛 󰇜
󰇛 󰇜 .............................................. 4
where  is the collector heat input “W”,  is the solar collector overall heat losses “W”, m is
the fluid mass flow rate (Kg/s), is the temperature of cold air “oK”, is the temperature of hot
air “oK”, Ta is the SC average temperature “oK”, Tm is the temperature of ambient still air oK”,
and is the air fluid heat capacity “kJ/kg °K”.
2.5.1.1 solar collector thermal losses
Because of the various layers and components, each of which has a different set of thermal
characteristics, it is challenging to measure the average solar collector temperature. as shown in
figure (4).
Figure 4: Heat transfer through layers of air, wood, glass wool and absorber plate.


................. 6
 ................................. 7
R overall = R glass wool+ R wood ....................................... 8
Tf
T1
T2
T3
T4
T5
Tm
x1
x2
x3
x4
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Page 323 Hassan et al., 2023
 .......................................................... 9
where R is the thermal resistance of insulation “°K/W”, R1 is the thermal resistance of
inner layer of insulation “°K/W”, R2 is the thermal resistance of second layer of insulation
“°K/W”, Rn is the thermal resistance of nth layer of insulation “°K/W”, RS is the thermal
resistance of outer surface of insulation “°K/W”, hb is the surface coefficient of outer surface
“W/m2 °K”, ha is the surface coefficient of inner surface “W/m2 °K”, kI is the thermal
conductivity of inner layer of insulation “W/m °K”, k2 is the thermal conductivity of second layer
of insulation “W/m° K”, and kn is the thermal conductivity of nth layer of insulation “W/m °K”.
According to earlier equations, a wooden frame and glass-wool layers were used to cover the
collector's back and sides in order to reduce heat losses from the FPC. The sum of the values for
the conductivity of air, wood, glass wool, and absorber layers will determine the heat transfer's
overall thermal conductivity (Awady, 1999).
2.5.2 Drying efficiency.
The ratio of energy used to heat the sample and evaporate its moisture to the total energy
consumed is known as drying efficiency. This gauges the dryer's overall efficacy.
(Forson et al., 2007; Drew, 2011 quoted from Brenndorfer et al, 1987).
………………………………………… (10)
Where;
Mw = Mass of moisture removed by dryer (kg)
T = total area of collectors (m2)
T = Average solar insolation (W/m2)
L = Latent heat of evaporation of water (kJ/kg)
Td = Overall drying time, (seconds)
2.5.3 Average drying rate.
The mass of moisture extracted by the drier, Mw, and drying time are used to calculate
the average drying rate, Mdr, the amount of moisture that was taken out of the meal over the
course of drying was given by (Tonui et al., 2014).

……………………………………………… (11)
Where,
dr = Average drying rate (kg/h)
Mw = Mass of moisture removed by dryer (kg)
Td = Overall drying time (h)
2.5.4 Moisture content.
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Page 324 Hassan et al., 2023
The amount of water in the produce is its moisture content. There are two methods for
calculating the moisture content of produce: on a wet basis and on a dry basis, the amount of
moisture in a material's original mass can be represented on a wet basis and expressed According
to (Mohanraj and Chandrasekar, 2009).
On wet basis
 󰇛󰇜
…………………………………… (12)
On dry basis, moisture
 
…………………..……………………………… (13)
Where,
wb= moisture content on wet basis (%)
db= moisture content on dry basis (%)
i = Initial mass of the product before drying (kg)
f = Final mass of the product after drying (kg)
2.5.4 Moisture gain or loss.
This is the percentage increase or decrease in moisture during the night period. A negative
value indicates further moisture loss while a positive value indicates moisture gain (Mohanraj
and Chandrasekar, 2009). It can be calculated as;

………………………………… (14)
Where;
sr = Mass at sunrise (kg)
ss = Mass at sunset (kg)
i = Initial mass of sample (kg)
2.6. Henna.
Lawsonia inermis L., sometimes known as henna bushes, is a member of the Lythraceae
family of plants, annual or perennial, with a lifespan of about three years and may extend to ten,
evergreen, abundantly branching, up to three meters long, and has roots and a red stake. henna
was obtained from one of the local fields in Aswan. Its stem has many branches and lateral
branches, and it is green in color. The shrub's height ranged from 2 to 3 meters, and the flower
color was Miniata with purple flowers. Leaves are dark oval, 1.5-5 cm long, and 0.5-2 cm wide.
Henna leaves contain different glycoside substances, the most important of which is the main
substance known as (Lawson) and its chemical molecule of the type 2-hydroxy-1,4-
naphthoquinone or 1,4-naphthoquinone. This substance is responsible for the biological effect in
medicine as well as the red dye.
Henna consists of the following compounds: Dyes of type 41-naphthoquinone, including
1% Lawson (2-hydroxy-41-naphthoquinone), hydroxylated naphthalene derivatives such as 4-
glucosyl and oxy-21-dihydroxy, cumarine,xanthon, flavonoids, 5-10% tannin,gallic acid, and a
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Page 325 Hassan et al., 2023
low amount of steroid like sitosterol The flowers contain a volatile oil that has a sweet and strong
smell, and its most important constituents are phobita ionones (A, B, and Ionone). The amount of
active substances, especially lawson (which is the colouring matter), increases in henna leaves as
the plant grows older, and young leaves contain small amounts of these substances compared to
their aged counterparts. Besides that, they contain gallic acid and tannins in a ratio of 510 And
sugary and resinous materials, at a rate of about 1%.
2.7 Experimental Procedures and Dryer Evaluation.
Fresh leaves of henna were obtained from one of the local fields in Aswan. The
extraneous elements, such as weeds and damaged or discolored plants, and the initial
moisture content of the henna leaves were determined by oven drying. The test was
conducted on September 13, 2022. Relative humidity, the temperature, the initial and final
mass of the henna leaves, and the speed of the wind were measured at various points
during the experiment.
2.7.1 Load test.
Under the solar drying test, 3000 g of henna leaves were used for the test. Each
tray was covered in a single layer of 1000g henna leaves. Additionally, the dryer's
evaluation criteria were noted. The original moisture content of henna leaves was
determined via oven drying, and the average value was 74%wb. The weight of the henna
leaves spread out on each tray was then calculated using the formula: [Tray + henna
leaves] - Tray = henna leaf weight. Trays containing the henna leaves were placed in the
drying chamber. Based on the established initial moisture content, the decrease in weight
of the henna leaves was measured and used to assess the moisture loss of the leaves
during the drying process. Wet basis calculations were used to determine the moisture
content at each point during the drying process. The henna leaves were dried further until
there was no discernible loss of weight or moisture. Based on the drying rate, drying
efficiency, and dryer's performance. Temperature and humidity are measured through a
humidity and temperature sensor.
3. Results and discussion.
3.1. Test.
The solar drying test was conducted on September 13, 2022, using the solar dryer to dry
the henna leaves. In this test, 3000 g of henna leaves in the form of two layers 1000 g in each
traywere dried over the course of nearly 7 daylight hours, going from a moisture content of
74.0% wb to a moisture content of 8.4% wb. A safe moisture content for storage is less than 10%
(Sengar et al., 2018).
3.1. Variation of Temperature with time.
Where the Temperatures with time were recorded, represented graphically as in Fig (5).
The plate of collector attained a maximum temperature of 70 °C, tray 1 in the drying
chamber recorded a temperature of 56.2 °C, and the ambint's average temperature was 42.21 °C
at 14 h. The ambient temperature and the dryer's average temperature were 37.2 and 43.84 °C,
respectively. A temperature increases of 5.01 o C above ambient resulted from this. The collector
attained a minimum temperature of 55 °C, tray 3's drying chamber recorded 39.5 °C, and the
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Page 326 Hassan et al., 2023
outside air temperature was measured at 28.08 °C at 8:00 a.m. It is also noted that the
temperatures on the first shelf are higher than on the second and third shelves, and on the second
shelf, they are higher than on the third shelf.
Figure (5). Variation of Temperature with time.
3.2. Variation of Moisture Content with time.
Where the Moisture Content with time were recorded, represented graphically as in Fig
(6). The experiment began with a moisture content of 74.0% w.b and ended with a moisture
content of 8.5% w.b in less than seven sunshine hours.
Figure (6). Variation of Moisture Content with time.
0
10
20
30
40
50
60
70
80
8 : A M 9 : A M 10A M 11AM 12P M 1 PM 2PM 3PM
temperature (0c)
time (hr)
tray 1 tray 2 tray 3 ambient T-plate
0
10
20
30
40
50
60
70
80
8AM 9AM 10AM 11AM 12PM 1PM 2PM 3PM 4PM
moisture content (%)
time (hr)
tray 1 tray 2 tray 3
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Page 327 Hassan et al., 2023
As observed in the graph, tray 1's sample lost water more quickly than trays 2 and 3's
samples did. It was noted that the moisture content steadily decreased over time after starting out
strongly. The correlation between drying rate and time-varying moisture content. the drying rate
gradually decreased from its initial high level as the moisture content decreased (Sengar et al.,
2018).
3.3. Variation of relative humidity with time.
Where the relative humidity with time were recorded, represented graphically as in Fig (7).
Figure (7). Variation of relative humidity with time.
Relative humidity vs time was plotted on the graph at three sections, at collector, ambient
air and in chamber of dryer from 8:00 a.m. to 3:00 P.M. at one-hour interval. Figure (7) shows at
first, it appeared that the relative humidity was nearly the same throughout. The relative humidity
started to drop as the air heated up in the solar collector, and it was typically around 8.6%. At
8:00 a.m., the relative humidity at the chamber outlet started to rise as a result of the hot air from
the collector entering the drying chamber evaporating moisture from the henna leaves. The
relative humidity starts to fall as the henna leaves start to dry, which means that the rate of
evaporation is slowing down with time. It is also noted that the relative humidity in the third shelf
is higher than in the first and second, and in the second shelf is higher than in the first shelf.
Thermal performance analysis of the solar collector system
1. Load
Table 5. Thermal performance analysis of the solar collector system.
Time
Solar energy
available
Absorbed
solar energy
Useful heaty
W
Solar collector
losses w
8:00
1083.74
848.77
800.28
48.49
9:00
1633.2
1279.12
1183
96.12
10:00
2058.16
1611.17
1477
134.17
11:00
2326
1821.7
1364
457.7
12:00
2417.47
1893.36
1595
298.9
13:00
2327.077
1822.56
1410
412.56
0
5
10
15
20
25
30
35
40
8AM 9AM 10AM 11A M 12PM 1PM 2PM 3PM
relative humidity(%)
time (hr)
tray 2 tray 3 ambient In Collector tray 1
Aswan University Journal of Environmental Studies (AUJES) 4 (5), pp. 315-332, (2023).
Online ISSN: 2735-4237, Print: ISSN 2735-4229. https://aujes.journals.ekb.eg/
Page 328 Hassan et al., 2023
Time
Solar energy
available
Absorbed
solar energy
Useful heaty
W
Solar collector
losses w
14:00
2057.9
1611.74
1356
255.74
15.00
1633.2
1279.12
1085.3
193.82
As shown (8).
Fig.(8): The absorbed solar energy, Solar energy available, heat losses, collection useful heat for
air as affected by time.
2.Noload
Table 6. Thermal Performance Analysis of the Solar Collector System.
Time
Solar energy
available
Absorbed
solar energy
Useful heat
K
Solar collector
losses
8:00
1096.3
858.62
769.5
89.12
9:00
1638.7
1283.4
900
383
10:00
2058.8
1612.45
1200
412
11:00
2324.97
1820.9
1200
620
12:00
2415.16
1891.55
1300
590
13:00
2324.97
1820.9
1698.4
122.5
14:00
2058.8
1612.45
1307.5
304
15.00
1638.7
1283.4
960
323.8
As shown (9).
0
500
1000
1500
2000
2500
3000
0
1000
2000
3000
4000
5000
6000
8:00 9:00 10:00 11:00 12:00 13:00 14:00 15:00
solar intensity (w/m2)
thermal analysis of collector (w)
time (hr)
Solar Intensity (W/M2 ) Absorbed solar energy (W)
Useful heaty (W) Solar collector losses (W)
Solar energy available (W)
Aswan University Journal of Environmental Studies (AUJES) 4 (5), pp. 315-332, (2023).
Online ISSN: 2735-4237, Print: ISSN 2735-4229. https://aujes.journals.ekb.eg/
Page 329 Hassan et al., 2023
Fig.(9): The absorbed solar energy, Solar energy available, heat losses, collection useful heat for
air as affected by time.
3. 3 Drying efficiency.
The drying efficiency of the dryer for the load test was evaluated at 19.5% for
solar drying. Given that the efficiency of the collector is far better than that of the dryer,
this solar collector could dry more leaves of henna in less time The greater the loading
density of the dryer, the higher its efficiency. This agrees with (Musembi et al., 2016).
In the case of favorable conditions during the load test of average temperature,
relative humidity, solar radiation, and flow rate within 7 hours, the maximum efficiency
of the dryer is equivalent to the efficiency of the solar collector, which is 79.7 %.
3.4. The effect of dryer efficiency on Lawsone pigment.
Lawsone chemical present in the aqueous extract of henna leaves was tested using the
TLC technique to determine the relative mobility (Rf) value. The RF value of the Lawson
compound is 0.4,
Which is identical to the standard value. This indicates that the compound is relatively
well bound to, or interacts with, the adsorbent, providing further ability to note differences
between the behavior of the target compound and other compounds. This is consistent with
Simon et al. (1984) If the Rf value is between 0.5 and 0.2, this represents that the compound is
relatively well bound or interacts with the adsorbent, providing further ability to note differences
between the behavior of the target compound and other compounds.
It was discovered that the degree of colour of the compound Lawson is close to the degree
of colour of the standard compound Lawson. This is proof of the excellent quality and substantial
amount of Lawson compound contained in the aqueous extract of dried henna leaves. Lawson is
the red orange hue and the primary colouring agent in henna, which is a reddish-orange molecule
(2-hydroxy-1,4 naptha quinone) that makes up 13% of the dry mass of dried leaves (Simon et
al., 1984).
0
200
400
600
800
1000
1200
0
2000
4000
6000
8000
8:00 9:00 10:00 11:00 12:00 13:00 14:00 15:00
solar intensity (w/m2 )
thermal analysis of collector(w)
time(hr)
Solar energy available(W) Absorbed solar energy (W)
Useful heat (W) Solar collector losses (W)
Total Solar Intensity w/m2)
Aswan University Journal of Environmental Studies (AUJES) 4 (5), pp. 315-332, (2023).
Online ISSN: 2735-4237, Print: ISSN 2735-4229. https://aujes.journals.ekb.eg/
Page 330 Hassan et al., 2023
Figure (10). TLC for test.
4. Conclusion.
During the load test, leaves of henna with an average initial moisture content of
74.0% wb were dried to an average moisture content 8.4% wb within 7 hours, depending
on the loading density of the product incorporating the lowest moisture content value. The
performance of the dryer was evaluated in terms of its efficiency and drying rate. Results
obtained from the test showed the collector efficiency for the load test was 80.5 percent.
Moreover, the drying efficiency for the load test was 19.5%. The drying rate was 306.7
g/h for the load test, and the solar radiation was 800 w/ m2. The maximum efficiency of
the dryer is equivalent to the efficiency of the solar collector, which is 79.7%, and
accordingly. According to the tests, it was observed that the efficiency The efficiency of
the collector is much higher than the efficiency of the dryer, so this solar collector can dry
more. It was possible to increase the efficiency of the dryer if the capacity was larger.
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