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Volume-7, Issue-5, September-October 2017
International Journal of Engineering and Management Research
Page Number: 125-139
Design and Fabrication of Solar Dryer for Sustainable Livelihoods of
Fisher Women
Debashree Debadatta Behera1, Biswajit Nayak
2, Shiv Sankar Das
3
1Sr. Lecturer, Mechanical Department, Centurion University of Technology and Management, Odisha, INDIA
2Associate Professor, Mechanical Department, Centurion University of Technology and Management, Odisha, INDIA
3Lecturer, MBA Department, Centurion University of Technology and Management, Odisha, INDIA
ABSTRACT Fisherwomen traditionally dry fish in open, often in
unhygienic conditions. It results in poor price realization
from the market. Application of solar drying technology has
the potential for higher value addition of fish products.
Accordingly, a solar dryer has been designed and fabricated
considering various system parameters such as inlet
temperature of air, humidity, moisture carried by air per
minute and outlet temperature of air. This dryer is being
used by the fisherwomen in coastal area of south Odisha
which is involved in technology based and market linked
sustainable livelihood security of fisherwomen. The dryer has
been designed with a capacity of 20 kg/day fish and is
manufactured with aluminium sheet and SS304 grade
stainless steel perforated trays. The present initiative relates
to an energy efficient solar dryer for drying foods, vegetables,
seafood, edibles or organic foods. More specifically, the
present set up eliminates moisture and provides sufficient
drying in a reliable, hygienic and economic way with all three
modes of heat transfer viz., conduction, convection and
radiation. Further, the present system eliminates the use of
auxiliary heaters by taking advantage of direct sunlight
falling over the dryer that is made of a good heat conducting
material to heat air within the drying room. The solar drying
device comprised of an enclosed means, a drying room,
plurality of perforated holders for holding of drying material
and a plurality for air blowing means powered by solar
energy in order to provide effective removal of moisture. The
perforation over the food holders is circular and the holders
are spaced at an equal distance from each other within the
drying room to facilitate effective air circulation. The air
blowing through fan is used to increase the rate of moisture
removal and circulation of heated air in the drying room. The
entire drying operation takes place by means of direct solar
energy falling over the dryer.
Keywords--- Solar energy; Moisture carrying capacity;
Relative humidity; PV panel; Hygienic
Nomenclature
=Mass of water to be removed
Mp = Mass of product
Mi = Initial water content in percentage
Mf = Final water content in percentage
Relative humidity
Partial pressure of water vapour
Partial pressure of water vapour when the air is
fully saturated
Atmospheric pressure
Specific humidity at inlet of dryer
Specific humidity at outlet of dryer
Mass of dry air in kg/hr
Mass of water vapour
RPM of fan
Volume of dry air
Volume of water vapour
Velocity of air inside the chamber
Velocity of the air at the outlet
Volume flow rate
Diameter of the fan
Transverse cross section area of dryer
Area of circular hole at outlet
Angular velocity
Length of the dryer
Width of the dryer
wM
vP
vsP
tP
1W
2W
am
vm
N
aV
vV
1v
2v
V
d
1A
2A
Lb
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I. INTRODUCTION
Solar drying technology involves exposing food
to sunlight, while air flowing past the food to remove the
moisture content from the food naturally. The warmer the
air, the more moisture it can remove from the food. The
present invention relates to an improved solar dryer with
improved air movement and warmth increasing the drying
efficiency.
We need a more simplified, easy to use, economic
and small scale direct solar dryer, which can utilize solar
energy for drying food as well as for powering of air
blowing units. A drying means which utilize all three
modes of heat transfer, conduction, convection and
radiation for enhanced drying to take place. The design
needs to affordable by the fishers for a better hygienic way
of drying food, thereby increasing the market value for
their effort.
Fisherwomen in coastal area find it difficult to
produce dried fish in a hygienic way. Exiting methods
available are expensive (electric drying), unreliable
(electricity is not available all the time) and unhygienic
(open sun drying). Given the availability of rich solar
energy for more than 80 percentage days in a year in
coastal area of Odisha, it can be used for drying fish.
Hence the present attempt will help fisherwomen in adding
higher value to their fish product and in the process getting
higher profit.
1.1 Development of Solar Drying
Solar drying is very important application of solar
energy. Solar dryers use air collectors to collect solar
energy. Solar dryers are used primarily by the agricultural
industry. The purpose of drying an agricultural product is
to reduce its moisture content to a level that prevents its
deterioration. In drying, two processes take place: one is a
heat transfer to the product using energy from the heating
source, and the other is a mass transfer of moisture from
the interior of the product to its surface and from the
surface to the surrounding air. Traditionally, farmers used
the open-to-the-sun or natural drying technique, which
achieves drying by using solar radiation, ambient
temperature, relative humidity of ambient air and natural
wind .The process (open-to-the-sun), however, has some
serious limitations. The most obvious ones are that the
crops suffer the undesirable effects of dust, dirt,
atmospheric pollution, and insect and rodent attacks. All
these disadvantages can be eliminated by using a solar
dryer.
All drying systems can be classified according to
their temperature range i.e. high temperature range dryer
and low temperature range dryer [1]. The solar dryers are
classified based on modes of air movement, exposure to
insulation, direction of air flow, arrangement of the dryer
and status of solar radiation [1]. Kainji Solar Tent Dryer
(KSTD) was constructed as an improvement of Doe’s tent
and the two solar tent dryers were used to dry fish [1].
Doua1,et al [2] have design and fabricated small-scale
drying equipment. These mechanisms are based on the
existence temperature gradient or pressure gradient
between the entry and the exit of the drying chamber.
Khoshmanesh et al [6] investigated a solar dehydrator for
the requirements of fish drying process such as minimum
moisture content, air temperature, air velocity, etc.
Murugappa et al [4] investigated a forced flow type dryer,
which consists of air heater, fan and drying chamber for
drying food products. YefriChana et al [17] have
developed a conventional flatbed dryer has the demerit of
having nonhomogeneous drying results.
1.1.1 Passive Solar Dryer
Passive solar dryers are also called natural
circulation or natural convection systems. They are
generally of a size appropriate for on-farm use. They can
be either direct (e.g. tent and box dryer) or indirect (e.g.
cabinet dryer). Natural-circulation solar dryers depend for
their operation entirely on solar-energy. The box-type is
one type of passive solar dryer which consists of a wooden
box with a hinged transparent lid. Another type of passive
solar dryer iscabinet solar dryer [1].
1.1.2 Active solar cabinet dryers
Active solar dryers are also called forced
convection or hybrid solar dryers. Optimum air flow can
be provided in the dryer throughout the drying process to
control temperature and moisture in wide ranges
independent of the weather conditions. The use of forced
convection can reduce drying time by three times and
decrease the required collector area by 50 %.
Consequently, dryer using fans may achieve the same
throughput as a natural convection dryer with a collector
six times as large [1].
1.2 Design and Fabrication of Solar Dryer
Khoshmanesh et al [6] developed a solar
dehydrator based on the dehydrating of 834kg fish (200 kg
fish without water) in period of 48 hour, for weather
condition of Brusher province in Iran has been designed.
Low temperature in the context of solar energy thermal
systems, generally applies to those applications, which
need energy at less than 100oC [6]. Also, as a corollary,
these applications also imply systems employing flat plate
collectors, though; there can be occasional exceptions. The
dryer consists of a flat plate solar collector and a chapel-
shaped greenhouse [6]. The drying rate in the solar
greenhouse dryer could be much higher than that for the
open air sun drying. Dryer is designed with a maximum
collector area of 1.5 m2, six crop trays with an effective
area of 0.50 _ 0.75 m2, can hold 12 kg of fresh leafy herbs.
[8]. The dryer is attached with a packed bed thermal
energy storage having capacity of 50 kg phase change
material (PCM). The drying system works in such a
manner that phase change material stores the thermal
energy during sun shine hours and releases the latent and
sensible heat after sunset, thus dryer is effectively
operative for next 5-6 h. The performance of a new design
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of a solar dryer for drying osmotically dehydrated cherry
tomatoes is presented [9]. The dryer consists of drying
cabinet, heat exchanger, 16-m2 water type solar collector,
and water type heat storage unit.David Gudiño-Ayala et al,
[16] presents the results of an experimental pineapple
(Ananas comosus L.) drying study in a new solar hybrid
dryer. The complete solar dryer was comprised of a feed
hopper, centrifugal blower, pneumatic conveyor and a
transparent structure acting as drying chamber containing a
hopper with vortex at the top. Pneumatic conveyor was
used to make recirculation of the grain and to perform
continuous drying process. Spherical model was used to
predict the drying time [17].
1.2.1 Geometric effect
The direction that a solar panel face is referred to as
its orientation. The orientation of the solar array is very
important as it affects the amount of sunlight hitting the
array and hence the amount of power the array will
produce. The orientation generally includes the direction
the solar module is facing (i.e. due south) and the tilt angle
which is the angle between base of the solar panel and the
horizontal. The amount of sunlight hitting the array also
varies with the time of day because of sun’s movement
across the sky. Solar module should be installed so that as
much radiation is collected as possible.
The purpose of a dryer is to supply more heat to the
product than that available naturally under ambient
conditions, thus increasing sufficiently the vapours
pressure of the crop moisture. Therefore, moisture
migration from the crop is improved. The dryer also
significantly decreases the relative humidity of the drying
air and by doing so, its moisture-carrying capability
increases, thus ensuring sufficient low equilibrium
moisture content. In this work the broad objective is to
develop an energy efficient solar dryer for drying foods,
vegetables, seafood in coastal area of Odisha.
II. DESIGN AND FABRICATION
In this work the solar dryer has been designed
considering various system parameters such as inlet
temperature of air, humidity, moisture carried by air per
minute and outlet temperature of air. The materials are
considered for various parts of the dryer and dryer is
fabricated by various processes.
2.1 Design calculations
For design calculations the considered dry bulb
temperatures (DBT) and relative humidity (RH) at inlet
and outlet are shown in figure 3.1. The parameters are
considered after a brief study of atmosphere at the coastal
area of south Odisha.
Figure 2.1. System parameters at inlet and outlet
Mp = 20 kg
Mi = 71%
Mf = 20%
=12.75 kg of water to be removed from 20 kg of wet fish (1)
At DBT = 36o C, RH = 63% (At Inlet)
(2)
kg of water per kg of dry air (3)
At DBT= 43o C, RH = 75% (At Outlet)
2.01
2.071.020
wM
vs
v
P
P
0594.063.0 vP
bar037471.0vP
vt
v
PP
PW
622.01
02387.0037471.00132.1
037471.0622.0
INLET
DBT = 36oC
RH=63%
OUTLET
DBT = 43oC
RH=75%
DRYING
CHAMBER
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(4)
kg per kg of dry air (5)
(6)
Assuming 10 hrs./day (in one day to be dried)
Mass of dry air per second, kg/sec
Volume flow rate of dry air,
m3/ sec (7)
(8)
Diameter of duct m =121 mm
Assuming 1.5 m/sec is the velocity of air inside the chamber
Velocity of air inside the chamber
Velocity of air inside the chamber = 0.068 m/sec (9)
2.2 Working principle
This unit consists of drying chamber and 10 watt
solar PV panel for converting solar radiation into
electricity (Fig. 2.2). This panel has been integrated with
dryer for powering 4 no of 12V DC fan that is two induced
draft fan and two forced draft fan. Further solar radiations
facilitate the drying operation to take place. Solar
radiations fall upon the dryer and heats up the device. The
dryer comprises of an enclosed means to open and close
the unit a plurality of food holding means arranged at
equal distances. Provisions are made at the side walls of
the dryer for a set of air blowing units powered by means
of solar photovoltaic cell. Plurality of blowers according to
the invention, assist in ingress and egress of air. Off the
plurality of blowers at the walls of the dryer a set of
blowers (forced draft fans) creates a positive pressure i.e.
above the atmospheric pressure are placed at the higher
side of the wall to ingress air into the unit across the food
vs
v
P
P
08649.075.0 vP
bar0648.0vP
vt
v
PP
PW
622.02
0425.00648.00132.1
0648.0622.0
12 WW
Mm w
a
airdryofkg3.68402387.00425.0
75.12
am
hourper air dryofkg4.6810
3.684am
019.03600
4.68am
vt
aaaa
PP
TRmV
510037471.00132.1
)36273(28701901.0
01727.0
5.14
2
11 dvAV
121.0d
2211 vAvA
5.1121.04
0.252
1
v
m/sec068.01 v
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holders, while the another set of blowers (induced draft
fan) are placed at the bottom of the wall of dryer to egress
air out of the unit. Further the fans provide proper
circulation of air within the drying room of the drying unit.
According to the design dry air is drawn into the unit by
means of set of air blowing units. The dryer being made of
a good heat conducting material, transfers heat
immediately to the dry air within the unit via convection.
Air blowing units; create convective air currents in the
drying chamber, circulating warm air in the entire drying
chamber. This warm air, passes across the food holders,
through the perforations on the food holders, thereby
drawing moisture from the food placed over the holders.
The dry, warm air absorbs moisture from the food,
becomes saturated moisture laden air. This saturated air is
withdrawn from the unit by another set of air blowing
units.
Figure 2.2. Schematic diagram of solar drying process using solar dryer
2.3 Physical size of the dryer
Length : 1000mm, Breadth : 500mm, Height :
500mm
Tray dimension : 980mm X 480mm, Tray equally
spaced : 100mm
Solar Panel: 10 W Panel (Vikram Solar)
2.3.1 Dimensions of the top, bottom and side frame
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Figure 2.3. Dimensions of the top, bottom and side frame.
Figure 2.4. Dimensions of back supporting frame and door frame.
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2.4 Specification for fabrication
The dimensions of the solar dryer has been
determined based on the system parameters such as flow of
air, capacity of dryer and moisture carried by dry air.
Capacity of solar dryer: 20 kg
Type of products to be dried: fish
No of trays used: 4
Length : 1000mm, Breadth : 500mm, Height :
500mm
Tray dimension : 980mm X 480mm, Tray equally
spaced : 100mm
Materials
Body of the dryer: Commercial grade Aluminium
(3mm)
Tray : Stainless steel of grade 304
Solar Panel: 10 W Panel (Vikram Solar)
2.5 Budget (BOQ) Proposal for Solar Dryer, Capacity of
20 KG
The broad objective of this Budget proposal is to
develop an affordable, reliable and high quality solar dryer
to be used for drying raw fish. The prototype is made by
aluminium sheets, S.S. sheet, angle bars (Specification
given). The total prototype constitute of three broad things
1) Aluminium sheets are cut as per the dimension by
shearing machine.
2) The frame and treys are fabricated as per the
dimension.
3) Sheets are drilled as per the dimension and joined
by riveting process.
4) Trays are drilled for proper airflow, 12V DC fans
are fixed in sideways for proper airflow into the
system and black paint is applied all over the
body.
2.6 Fabrication process
The dryer has been fabricated with the help of
aluminium sheets, S.S. Bolts, Angle bars. The various
parts of the dryer have been fabricated by various
processes. The fabrication is explained below.
Sheet Metal Cutting: Sheets are cut to the
dimension of top and bottom frame, side frame, back
supporting frame and four trays by shearing process. The
frames are joined by riveting process. Since Aluminum
welding process is not available here. To fix the 12V DC
fan four holes of diameter 120 mm are made by drilling
process. These fans are fixed in sideways for proper
airflow into the system. Trays are perforated for proper
airflow and placed inside the dryer at equal space. To keep
the trays the angle bars are fixed on the side frame of the
dryer. The fabrication of different parts of dryer is shown
in figure 2.5. The figure 2.6 shows the complete dryer and
the solar panel.
Table 2.1: Bill of Materials and Estimated Price.
Item
no Description of item Unit Quantity Total
Total
Cost
1 Aluminium sheets Sq.
Length=1000m
m,
Width=1000m
m, Height=
500mm
27 Sq. 12000/-
2 Tray will be made of
Al Sq.
980mm x
480mm 5.06 Sq. 6500/-
3 S.S. Bolts Nos M6/10mm 50nos 500/-
4 NUTS Nos M4/10mm 30nos 500/-
5 NUTS Nos M3/10mm 12nos 500/-
6 L-Angle for Foot
Support Nos L-Angle 4nos 500/-
7 Red-Oxide -- 0.5 L -- 500/-
8 Solar Panel PC 60W, 12VDC -- 3000/-
9 Fans PC 12V DC Fan 4nos 5000/-
10 Copper Wires m 5 m -- 1000/-
Total
30000/-
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Figure 2.5. Fabrication of different parts of solar dryer by various processes
Figure 2.6. Dryer and solar panel
2.7 Installation of Photo Voltaic panel
The figure 2.7 shows the solar tracking frame
which is installed in order to make the module facing
towards the sun at all times. Because the amount of
sunlight hitting the array also varies with the times of days
because of the sun’s movement across the sky. As the
Gopalpur latitude is 19o18
’13.44”N/84
o57’52.72”E, the
panel was tilted 19o facing towards south.
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Figure 2.7. The installation of PV panel
III. RESULTS AND DISCUSSIONS
In this chapter the experiments on the solar dryer
have been conducted. 20 kg of different types of fishes
have been taken for the experiment.
3.1. Inside Temperature of Dryer
To measure the inside temperature, the dryer is
kept in a open field so that the dryer can be exposed to sun
ray. For the experiment the considered parameters are
presented in the table 3.1. The experiment is started at 9
am and at every one hour interval the inside temperatures
are measured by non-contact type pyrometer. The
temperatures obtained from the experiment are shown in
the table 3.2.
Table 3.1. Various Parameters Considered for Experiment.
Name of the Product Fish (Kana Katha) - Indian Mackerel
Zoological Name Rastrelliger Kanagutra
Month May
Starting Hour 9.00 am
Ending Hour 4.00 pm
Total Weight Before Drying 4000 gm.
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Weight of the fish tested in solar dryer 2000 gm.
Weight of the fish tested in Traditional Direct
Sunlight drying 2000 gm.
From the table 3.2 it has been observed that the
inside temperature of the solar dryer increases with time,
up to 2 pm and then decreases. It happens due to the
increase of sun ray and the black coating on the solar
dryer. Due to increase in temperature the moisture carrying
capacity of the air increases and accordingly the
performance of the dryer increases. With increase in
temperature of air the relative humidity reduces and the
warm air absorbs moisture from food, become saturated
moisture air. The temperature variations are shown in
figures 3.1 to 3.3.
Table 3.2. Inside temperature of the solar dryer
Figure 3.1. Temperature measurement in o C inside the dryer on Day-1
34.3 38
43
47
51 50 48
44
34 35.6
37.7 38 39 37 36 35
20
25
30
35
40
45
50
55
60
8 9 10 11 12 13 14 15 16 17
Dry
er t
emp
era
ture
(O
C)
Time (hrs)
temp inside thedryer(oC)
Atmospherictemperature (o C)
Day / Time 9 am 10 am 11 am 12
Noon 1 pm 2 pm 3 pm 4 pm
Day-1
Temp inside
the Dryer
34.3°C 38°C 43°C 47°C 51°C 50°C 48°C 44°C
Atm. Temp 34°C 35.6°C 37.7°C 38°C 39°C 37°C 36°C 35°C
Day-2
Temp inside
the Dryer
36°C 38°C 42.7°C 47.7°C 54°C 50°C 48°C 40°C
Atm. Temp 35°C 36°C 38°C 40°C 39°C 37°C 34°C 33°C
Day-3
Temp inside
the Dryer
37°C 40°C 44.7°C 50°C 55°C 48°C 46°C 44°C
Atm. Temp 36°C 38°C 39°C 40°C 39.5°C 38°C 37°C 35°C
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Figure 3.2. Temperature measurement in
oC inside the dryer as on Day-2
Figure 3.3. Temperature measurement in
oC inside the dryer as on Day-3
3.2. Temperature variation in Four Trays
To measure the inside tray temperature, the same
parameters shown in table 3.1 have been considered and
the temperatures are measured. The temperatures measured
from the experiment are shown in the table 3.3. It has been
found that there is a small variation in temperature from
tray 1 to tray 4 as per the thermodynamics second law heat
always flow from higher temperature to lower
temperature.The temperature variations are shown in
figures 3.4 to 3.6.
36 38
42.7
47.7
54
50 48
40
35 36 38
40 39 37
34 33
20
25
30
35
40
45
50
55
60
8 9 10 11 12 13 14 15 16 17
Dry
er t
emp
era
ture
(o
C)
Time (hrs)
Temp inside thedryer (o C)
Atmospherictemperature (o C)
37
40
44.7
50
55
48 46
44
36 38 39 40 39.5
38 37 35
20
25
30
35
40
45
50
55
60
8 9 10 11 12 13 14 15 16 17
Dry
er
tem
pe
ratu
re (
o C
)
Time (hrs)
Temperatureinside thedryer (o C)
Atmospherictemperature(o C)
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Table 3.3. Different temperature at different trays
Figure 3.4. Temperature of Different trays on Day-1
30
40
50
60
8 9 10 11 12 13 14 15 16 17
Tem
p e
ratu
re (
o C
)
Time (hrs)
Tray 1
Tray 2
Tray 3
Tray 4
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Figure 3.5. Different temperature of trays on Day-2
Figure 3.6. Different temperature of trays on Day-3
3.3 Testing of Dryer
To study the performance of the dryer, varieties
of fishes have been dried. The figure 3.7 shows the drying
of fish in the solar dryer. The table 3.3 shows the
comparison of weight reduction of fish dried in open
sunlight and dried in solar dryer. It can be seen that the
percentage of weight reduction is more in case of dryer
with a less time.
30
40
50
60
8 9 10 11 12 13 14 15 16 17
Tem
pe
ratu
re (
o C
)
Time (hrs)
Tray 1
Tray 2
Tray 3
Tray 4
30
40
50
60
8 9 10 11 12 13 14 15 16 17
Tem
per
atu
re (
o C
)
Time (hrs)
Tray 1
Tray 2
Tray 3
Tray 4
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Table 3.4. Weight of fish before and after drying:
Fish Initial Weight
(gm.)
Final Weight
(gm.)
Time Taken
(Hrs.)
Weight
Reduction %
Dried in Open
Sunlight 2000 903.24 56 54.8
Dried in Solar Dryer 2000 757.9 21 62.01
Figure 3.7. Varieties of fishes during drying operation
IV. CONCLUSIONS
Solar dryer according to the design eliminates
unhygienic traditional way of drying food in open lands
receptive to contaminants. Further the enhanced dryer,
eliminates large place for drying, further being provided
with holders that has enough capacity for large amounts of
food to be dried. The enhanced solar dryer improves
drying efficiency resulting in increased market value to the
products. Conventional method of drying small prawns has
a market value of 350 INR per kg while the solar dried
prawns’ sale has 70% over conventional methods pricing
up to 450 INR. Solar drying technology involves exposing
food to sunlight, while air flowing past the food to remove
the moisture content from the food naturally. The warmer
the air, the more moisture it can remove from the food.
The solar dryer of the present work facilitates quick drying
of the material to be dried. It can be seen that the
percentage of weight reduction is more in case of dryer
with a less time as compare with the fish dried in open
sunlight. The temperature inside the drying chamber
increases up to 51o
C while the atmospheric temperature is
34o C so that the efficiency of the dryer increases. It works
throughout the year. It can work at night and during rainy
season by burning biomass under the dryer. During
daytime it can be heated up by direct solar radiation. It can
be easily assembled and disassembled. It is light weight for
transportation purpose and also low maintenance cost.
REFERENCES
[1] Weiss, W. and Buchinger, J. , Solar drying,www.aee-
intec.at/0uploads/dateien553.pdf
[2] Doua, P., Kapseu, C. and Kuitche, A. (2014). An
Overview of Moisture Removal Mechanisms in Small-
scale Dryers. International Journal of Research Studies in
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