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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1643
Automation of Solar Tunnel Dryer using Arduino For Sapota
Miss. Shilpa B. Mali1 and Prof. M. C. Butale2
1 Student of Department of Electrical Engineering
2 Associate professor of Department of Electrical Engineering
Padmbhooshan Vasantraodada Patil Institute of Technology, Budhgaon
-----------------------------------------------------------------***----------------------------------------------------------------
ABSTRACT:- Sun drying of agricultural products is the
traditional method employed in most of the developing
countries. Sun drying is used to denote the exposure of a
commodity to direct solar radiation and the convective
power of the natural wind. Solar drying can be considered
as an advancement of natural sun drying and it is a more
efficient technique of utilizing solar energy due to it’s
renewable, environmentally friendly technology.
Nowadays drying agricultural products have great
attention and there are various methods of drying fruits,
vegetables such as dehydration, canning etc. due to this the
quality of such product is degraded so solar dryer is used
to avoid wastage, increase the productivity of agriculture,
also the production in terms of quality and quantity. This
project describes a controlled environment which is
suitable for small scale agricultural products drying
process within a closed chamber, using Arduino. To start
with, the sun rays are used to internally heat the fruit to
remove the water content within the agricultural products.
Then to maintain the humidity below a specified level,
exhaust the humid air out of the chamber. Arduino is used
to control the functions of heating, controlling the speed of
exhaust fan and giving time indication & maintain constant
temperature throughout the chamber. The graphs of time
versus drying process obtained show that the automatic
drying unit designed has worked as per the expectation by
consuming less time compared to conventional drying
process.
Keywords : Arduino, Sensor, Foldable Solar Dryer, LCD
Display.
INTRODUCTION
Drying is an excellent way to preserve food and solar food
drying is an appropriate food preservation technology for
a sustainable world. The high moisture content in fresh
agricultural product (produce) is the basic cause for
spoilage. If water is removed, then the shelf life of produce
increases. Traditional open sun drying methods often yield
poor quality, since the produce is not protected against
dust, rain and wind, or even against insects, birds, rodents
and domestic animals while drying. The solution of all
these problems is the use of solar dryer instead of open
sun drying.
Solar dryers are the devices that use free solar energy to
dry agro products. The studies indicate that cost of drying
with solar energy is only one-third as compared to the cost
using a dryer based on conventional fuels. Adequate
drying helps to preserve the flavor, texture, and color of
the food, which leads to a better quality product.
In India, sapota is cultivated over an area of 156.1
thousand hectares with annual production of 13.08 lacs
MT. Sapota is widely cultivated in Gujrat, West Bengal,
Karnataka, Andhra Pradesh, Maharashtra and Tamil Nadu.
It is highly perishable fruit with moisture content of 70-
80% which can be reduced down to 10% by drying in
order to increase the shelf life. Mostly used methods for
drying agricultural products like Sapota are canning,
osmotic dehydration, microwave drying, oven drying,
vacuum drying etc. due to this the quality of such product
is degraded so solar dryer is used to avoid wastage,
increase the productivity of agriculture, also the
production in terms of quality and quantity. Different food
types require different temperature for drying conditions
in order to maintain their quality. In solar tunnel dryer we
can not control various drying parameters like
temperature, relative humidity etc. due to that quality and
quantity of product degraded. To overcome this problem
we can use automatically controlled solar tunnel dryer.
The temperature inside the solar tunnel dryer can be
controlled by using microcontrollers like 8051, PIC, ARM,
Arduino etc These solar dryers allow for controlled drying
by managing the drying parameters such as moisture
content, air temperature, humidity, and air flow rate.
METHODOLOGY
The design used for agro products drying chamber needs
the temperature to be controlled throughout the drying
process by using solar energy. Variable temperature
conditions during drying are harmful for agro products.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1644
Over drying causes discoloration and reduction in quality.
On the other hand, under drying causes fungal infection
and bacterial action. Thus main objectives are to design
the solar tunnel dryer and to design a controlling circuit to
control various drying parameters inside it.
1) Solar Tunnel Dryer:
The material used for construction of folding type small
size passive solar tunnel dryer is given in the following
table 1:
Table 1: Material required for solar tunnel dryer
Sr.
No.
Item
Specification/
Quantity
1. GI bar 8.92 m
2. GI Sheet 26 gauge
3. PVC pipe 5.49 m
4. UV stabilized
polythene sheet,
thickness 200
microns
5 × 5 m2
5. Insulation(Plywood
)
2
6. Binder clips 28
The schematic design of solar tunnel dryer is shown in fig
1:
All dimensions in mm
Fig. 1: Schematic Diagram of Solar Tunnel Dryer
2) Solar Tunnel Dryer with controlling circuit:
The above Solar Tunnel Dryers parameters are tested and
controlled using Arduino as shown below
BLOCK DIAGRAM
Fig. 2: Block diagram of solar tunnel dryer
CIRCUITRY
1. Arduino Uno
Table 2: Specifications of Arduino Uno
Operating Voltage 5V
Input Voltage 7-12V
Digital I/O Pins 14
Analog Input 6 Pins
Length 68.6 mm
Width 53.4 mm
Weight 5
2. Temperature Sensor LM 35
Table 3: Specifications of Temperature Sensor LM 35
Supply Voltage +35 V to -0.2 V
Output Voltage +6 V to -1 V
Temperature Range -55 °C to 150 °C
3. Relay
Table 4: Specifications of Relay
Operating Voltage 5 V DC
Nominal current 70 mA
Quantity 2
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1645
4. Liquid Crystal Display
Table 5: Specifications of Liquid Crystal Display
Operating Voltage 5 V DC
Module Dimension 60 mm x 36 mm x 15 mm
Viewing Area Size 64.5 mm x 16 mm
Displays 2 lines x 16 characters
5. Exhaust Fan
Table 6: Specifications of Exhaust Fan
6. Solar Panel
Table 7: Specifications of Solar Panel
Rated Power 10 Watt
Open circuit voltage (Voc) 21.5 Volt
Short circuit current (Isc) 0.65 Ampere
Voltage at maximum power
(Vmp)
17.7 Volt
Current at maximum power
(Imp)
0.57 Ampere
Maximum system voltage 600 Volt
7. Battery
Table 8: Specifications of Battery
Voltage 12 Volt
Capacity 7 Ah
Type Sealed Lead Acid Battery
Rechargeable Yes
8. Charge controller
Table 9: Specifications of Charge Controller
Voltage 12 Volt
Max. PV charging Current 5 Ampere
Max. load 5 Ampere
Fig. 3: Actual View of circuit diagram
The measurements of the parameters were taken
after every half hour.
Table : 10 Parameters measured and instruments
used
Parameter Instrument
Temperature
Digital
Thermometer
Relative
Humidity
Hygrometer
Air Velocity Digital Anemometer
Solar Radiations Pyranometer
Flow chart of Sapota drying is given below :
Fig. 4: Flow chart of drying Sapota
Operating
Voltage
5 V
Dimension 100 × 100 mm × 10 mm
Selection of Sapota
Sorting
Cleaning
Drying
Weighing
Cutting / slicing if
required
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1646
Flow chart of controlling Solar Tunnel Dryer is given
below:
The effect of drying air temperature that is
50ºC on drying kinetics of Sapota slices was investigated
using solar tunnel dryer.
Determination of Moisture Content:
( )
Where,
W₁=Weight of sample before drying, g.
W₂=weight of sample after drying, g.
Determination of Drying efficiency:-
Drying efficiency % ( )
Where,
W= mass of moisture evaporated (kg) in
time ‘t’
∆H₁= Latent heat of evaporation (kJ/kg)
Ic = Isolations on collector surface (kW/m2)
Ac = Collector area, m2
RESULT AND DISCUSSION
Evaluation of Solar Tunnel Dryer for No load condition
Evaluation and testing of the Solar Tunnel Dryer
was carried out under no load conditions.
Fig. 5 Variation of Temperature, Humidity and Solar
Radiation with Time at No load condition
It was observed that the minimum inside temperature was
25.70C at 8:00 am and also observed that the minimum
and maximum dryer humidity was 20 % and 32% from
08:00 am to 5:00 pm respectively. The minimum and
maximum base temperature is 25.70C at 08:00 am and
63.20C at 1:30 pm respectively. The minimum solar
radiation was observed at 08:00 am and maximum at 1:00
pm were 189 and 1008 W/m2 respectively.
Fig. 5 clearly explains the minimum and maximum
temperature of dryer, ambient temp, humidity, solar
radiation. It was observed that the minimum and
maximum ambient temperature of air was observed at
8:00 am and 01:30 pm that is 25.00C and 36.20C
respectively.
Fig. 6 Variation of Air Flow Velocity with Time at No
load condition
Fig. 6 shows that the variation of air flow velocity of wind
velocity with respect to time. The minimum & maximum
air flow velocity was observed at 09:00 am and 01:30 pm,
0.03 m/s and 2.25 m/s respectively.
0
500
1000
1500
0
20
40
60
80
8:00
10:00AM
12:l00…
2:00PM
4:00PM
SolarRadiations
Temperature&RH
Time
Ambie
nt
Temp.
T1 (
Top )
0
1
2
3
8:00AM
9:00AM
10:00AM
11:00AM
12:00Noon
1:00PM
2:00PM
3:00PM
4:00PM
5:00PM
AirandWindVelocity
Time
Air and wind velocity
Air and wind velocity
Set Temperature
If Temperature ˃ Set
Temperature
FAN is ON
FAN is OFF
Yes
No
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1647
Evaluation of Solar Tunnel Dryer for Sapota
Evaluation and testing of the Solar Tunnel Dryer was
carried out under load conditions for drying of sapota
slices.
Fig. 7 Variation of Temperature, Humidity and Solar
Radiation with Time at 1st Day
On the first day of drying it was observed that the
minimum inside temperature was 27.80C at 8:00 am. It
also observed that the minimum and maximum dryer
humidity was 20 % and 32 % from 08:00 am to 5:00 pm
respectively.
The minimum and maximum base temperature is 29.20C
at 08:00 am and 52.640C at 12:00 noon. The minimum
solar radiation was observed at 08:00 am and maximum at
12:00 noon were 169 and 995 W/m2 respectively.
Fig. 7 clearly explains the minimum and
maximum temperature of dryer, ambient temp, humidity,
solar radiation. It was observed that the minimum and
maximum ambient temperature of air was observed at
8:00 am and 01:30 pm that is 25.20C and 34.10C
respectively.
Fig. 8 Variation of Air Flow Velocity with Time at 1st
Day
Fig. 8 shows that the variation of air flow velocity
of wind velocity with respect to time. The minimum and
maximum air flow velocity was observed at 09:00 am and
03:00 pm i.e. 0.03 m/s and 1.44 m/s respectively.
Fig. 9 Variation of Temperature, Humidity and Solar
Radiation with Time at 2nd Day
On the second day of drying it was observed that
the minimum inside temperature was 29.40C at 8:00 am
and also observed that the minimum and maximum dryer
humidity was 20 % and 32 % from 08:00 am to 5:00 pm
respectively. The minimum and maximum base
temperature is 30.20C at 08:00 am and 51.170C at 12:00
noon. The minimum solar radiation was observed at 08:00
am and maximum at 12:30 noon were 153 W/m2 and
1019 W/m2 respectively.
Fig. 9 shows the minimum and maximum
temperature of dryer, ambient temp, humidity, solar
radiation. It was observed that the minimum and
maximum ambient temperature of air was observed at
8:00 am and 1:30 pm i.e. 25.20C and 38.50C respectively.
Fig. 10 Variation of Air Flow Velocity with Time at 2nd
Day
Fig. 10 shows that the variation of air flow
velocity of wind velocity with respect to time. The
minimum and maximum air flow velocity was observed at
03:00 pm and 10:00 am i.e. 0.03 m/s and 1.17 m/s
respectively.
0
500
1000
1500
0
20
40
60
8:00AM
10:00AM
12:00…
2:00PM
4:00PM
Solar
Radiation(W/mˆ2
)
Temperature(◦C)
&RH(%)
Time(hr)
Ambien
t Temp.
T1 (top)
0
1
2
8:00AM
9:30AM
11:00AM
12:30PM
2:00PM
3:30PM
5:00PM
Airandwind
velocity(m/s)
Time(hr) Air and wind…
0
1
2
Airandwind
velocity(m…
Time(hr) Air and wind…
0
200
400
600
800
1000
1200
0
10
20
30
40
50
60
8:00AM
10:00AM
12:00Noon
2:00PM
4:00PM
SolarRadiation(W/mˆ2)
Temperature(◦C)&RH(%)
Time (hr)
Ambie
nt
Temp.
T1
(top)
T2
(middl
e)
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1648
Fig. 11: Sapota
slices
before drying
Fig. 12: Sapota slices
after drying
Determination of Moisture Content
Table 11: Initial Moisture Content
Weigh
t of
empty
box
gm
Weight of
empty box
+ Weight of
sample
before oven
drying (W2)
gm
Weight of
empty box
+ Weight
of sample
after oven
drying
(W3) gm
Moistu
re
conten
t %
(wet
basis)
59.3 64.16 60.6 73.25
Table 12: Moisture Content after 1st Day
Weight of
empty box
gm
Weight of
empty box +
Weight of
sample
before oven
drying (W2)
gm
Weight of
empty box
+ Weight of
sample
after oven
drying
(W3) gm
Moisture
content %
(wet basis)
59.3 63.52 62.39 26.72
Table 13: Moisture Content after 2nd Day
Weight of
empty box
gm
Weight of
empty box +
Weight of
sample
before oven
drying (W2)
gm
Weight of
empty box
+ Weight of
sample
after oven
drying
(W3) gm
Moisture
content %
(wet basis)
59.3 63.69 63.24 10.22
Fig. 13: Removal of moisture from sapota per day
From the fig. 13 it is observed that sapota require
2 days for drying. The drying rate is high. It is found that
the initial moisture content of Sapota Slices was 73.25%
which was reduced to 26.72 % on first day and on next
day it was reduced to 10.22%.
CONCLUSION
Using the concept of basic solar conduction dryer
and implementing the automation and design
enhancement, the efficiency of the system and quality of
agro products has been increased. By utilizing large
amount of solar heat to maintain the quality of the food
products is also achieved. From the experiment performed,
the dryer accomplishes the temperature control at desired
temperature.
The overall reading observed that the
maximum inside temperature was 520C. Corresponding
average ambient temperature was 32.520C. It was also
observed that the average solar radiation was 787.52
W/m2, average humidity was 20 % and average the air
flow velocity was 0.89 m/s. The initial moisture content of
Sapota slices was 73.25% which was reduced to 26.72% in
1 day and on next day it was reduced to 10.22%.
REFERENCES
1. Bagh, S., Shrivastava, A., Singh, A. V., Shrivastava,
A. C., Gupta L., 2015. Review on Design of
temperature controlled solar dryer. International
Journal of Advanced Research in Electrical,
Electronics and Instrumentation Engineering,
4(11):8731-8740
2. Dangi, N., 2017. Review on Monitoring
environmental parameters: humidity and
0
10
20
30
40
50
60
70
80
Initial Day 1 Day 2
Moisture Content
Moisture
Content
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1649
temperature using Arduino based microcontroller
and sensors.
3. Gupta, S. V., Patil, B. N., 2014. Connective drying of
osmo-dehydrated sapota slices. International
journal of agriculture and food science technology,
5(2); 219-226.
4. Hegde, V. N., Hosur, V. S., Rathod, S. K., Harsoor, P.
A. and Badari, N., 2015. Review on Design,
fabrication and performance evaluation of solar
dryer for banana. Energy, Sustainability and
Society Journal.
5. Louis, L. 2016. Review on Working principle of
Arduino and using it as a tool for study and
research, International Journal of Control,
Automation, Communication and System (IJCACS),
1(2):21-29.
6. Moloney, C., 2016. India's major agricultural
produce losses. [Online]. Available:
https://www.firstpost.com/business/indias-major-
agricultural-produce-losses-es timated-at-rs-
92000-cr-2949002.html [Accessed on 30-July-2018]
7. Singh, D., Meena, M. L., Chaudhary, M., Dayal, H.
and Dudi, A., K., 2004. Review on Local Solar
Tunnel Dryer for Small Scale, Entrepreneurship in
Rural India, Central Arid, Zone Research Institute,
Pali, Rajasthan, India. : 10-21.
8. Vardini, P. S., Hegade, V. N., Panvare, N. L., 2016.
Design and Performance Evaluation of Solar
Tunnel Dryer 9(3):955-967.

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IRJET- Automation of Solar Tunnel Dryer using Arduino for Sapota

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1643 Automation of Solar Tunnel Dryer using Arduino For Sapota Miss. Shilpa B. Mali1 and Prof. M. C. Butale2 1 Student of Department of Electrical Engineering 2 Associate professor of Department of Electrical Engineering Padmbhooshan Vasantraodada Patil Institute of Technology, Budhgaon -----------------------------------------------------------------***---------------------------------------------------------------- ABSTRACT:- Sun drying of agricultural products is the traditional method employed in most of the developing countries. Sun drying is used to denote the exposure of a commodity to direct solar radiation and the convective power of the natural wind. Solar drying can be considered as an advancement of natural sun drying and it is a more efficient technique of utilizing solar energy due to it’s renewable, environmentally friendly technology. Nowadays drying agricultural products have great attention and there are various methods of drying fruits, vegetables such as dehydration, canning etc. due to this the quality of such product is degraded so solar dryer is used to avoid wastage, increase the productivity of agriculture, also the production in terms of quality and quantity. This project describes a controlled environment which is suitable for small scale agricultural products drying process within a closed chamber, using Arduino. To start with, the sun rays are used to internally heat the fruit to remove the water content within the agricultural products. Then to maintain the humidity below a specified level, exhaust the humid air out of the chamber. Arduino is used to control the functions of heating, controlling the speed of exhaust fan and giving time indication & maintain constant temperature throughout the chamber. The graphs of time versus drying process obtained show that the automatic drying unit designed has worked as per the expectation by consuming less time compared to conventional drying process. Keywords : Arduino, Sensor, Foldable Solar Dryer, LCD Display. INTRODUCTION Drying is an excellent way to preserve food and solar food drying is an appropriate food preservation technology for a sustainable world. The high moisture content in fresh agricultural product (produce) is the basic cause for spoilage. If water is removed, then the shelf life of produce increases. Traditional open sun drying methods often yield poor quality, since the produce is not protected against dust, rain and wind, or even against insects, birds, rodents and domestic animals while drying. The solution of all these problems is the use of solar dryer instead of open sun drying. Solar dryers are the devices that use free solar energy to dry agro products. The studies indicate that cost of drying with solar energy is only one-third as compared to the cost using a dryer based on conventional fuels. Adequate drying helps to preserve the flavor, texture, and color of the food, which leads to a better quality product. In India, sapota is cultivated over an area of 156.1 thousand hectares with annual production of 13.08 lacs MT. Sapota is widely cultivated in Gujrat, West Bengal, Karnataka, Andhra Pradesh, Maharashtra and Tamil Nadu. It is highly perishable fruit with moisture content of 70- 80% which can be reduced down to 10% by drying in order to increase the shelf life. Mostly used methods for drying agricultural products like Sapota are canning, osmotic dehydration, microwave drying, oven drying, vacuum drying etc. due to this the quality of such product is degraded so solar dryer is used to avoid wastage, increase the productivity of agriculture, also the production in terms of quality and quantity. Different food types require different temperature for drying conditions in order to maintain their quality. In solar tunnel dryer we can not control various drying parameters like temperature, relative humidity etc. due to that quality and quantity of product degraded. To overcome this problem we can use automatically controlled solar tunnel dryer. The temperature inside the solar tunnel dryer can be controlled by using microcontrollers like 8051, PIC, ARM, Arduino etc These solar dryers allow for controlled drying by managing the drying parameters such as moisture content, air temperature, humidity, and air flow rate. METHODOLOGY The design used for agro products drying chamber needs the temperature to be controlled throughout the drying process by using solar energy. Variable temperature conditions during drying are harmful for agro products.
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1644 Over drying causes discoloration and reduction in quality. On the other hand, under drying causes fungal infection and bacterial action. Thus main objectives are to design the solar tunnel dryer and to design a controlling circuit to control various drying parameters inside it. 1) Solar Tunnel Dryer: The material used for construction of folding type small size passive solar tunnel dryer is given in the following table 1: Table 1: Material required for solar tunnel dryer Sr. No. Item Specification/ Quantity 1. GI bar 8.92 m 2. GI Sheet 26 gauge 3. PVC pipe 5.49 m 4. UV stabilized polythene sheet, thickness 200 microns 5 × 5 m2 5. Insulation(Plywood ) 2 6. Binder clips 28 The schematic design of solar tunnel dryer is shown in fig 1: All dimensions in mm Fig. 1: Schematic Diagram of Solar Tunnel Dryer 2) Solar Tunnel Dryer with controlling circuit: The above Solar Tunnel Dryers parameters are tested and controlled using Arduino as shown below BLOCK DIAGRAM Fig. 2: Block diagram of solar tunnel dryer CIRCUITRY 1. Arduino Uno Table 2: Specifications of Arduino Uno Operating Voltage 5V Input Voltage 7-12V Digital I/O Pins 14 Analog Input 6 Pins Length 68.6 mm Width 53.4 mm Weight 5 2. Temperature Sensor LM 35 Table 3: Specifications of Temperature Sensor LM 35 Supply Voltage +35 V to -0.2 V Output Voltage +6 V to -1 V Temperature Range -55 °C to 150 °C 3. Relay Table 4: Specifications of Relay Operating Voltage 5 V DC Nominal current 70 mA Quantity 2
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1645 4. Liquid Crystal Display Table 5: Specifications of Liquid Crystal Display Operating Voltage 5 V DC Module Dimension 60 mm x 36 mm x 15 mm Viewing Area Size 64.5 mm x 16 mm Displays 2 lines x 16 characters 5. Exhaust Fan Table 6: Specifications of Exhaust Fan 6. Solar Panel Table 7: Specifications of Solar Panel Rated Power 10 Watt Open circuit voltage (Voc) 21.5 Volt Short circuit current (Isc) 0.65 Ampere Voltage at maximum power (Vmp) 17.7 Volt Current at maximum power (Imp) 0.57 Ampere Maximum system voltage 600 Volt 7. Battery Table 8: Specifications of Battery Voltage 12 Volt Capacity 7 Ah Type Sealed Lead Acid Battery Rechargeable Yes 8. Charge controller Table 9: Specifications of Charge Controller Voltage 12 Volt Max. PV charging Current 5 Ampere Max. load 5 Ampere Fig. 3: Actual View of circuit diagram The measurements of the parameters were taken after every half hour. Table : 10 Parameters measured and instruments used Parameter Instrument Temperature Digital Thermometer Relative Humidity Hygrometer Air Velocity Digital Anemometer Solar Radiations Pyranometer Flow chart of Sapota drying is given below : Fig. 4: Flow chart of drying Sapota Operating Voltage 5 V Dimension 100 × 100 mm × 10 mm Selection of Sapota Sorting Cleaning Drying Weighing Cutting / slicing if required
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1646 Flow chart of controlling Solar Tunnel Dryer is given below: The effect of drying air temperature that is 50ºC on drying kinetics of Sapota slices was investigated using solar tunnel dryer. Determination of Moisture Content: ( ) Where, W₁=Weight of sample before drying, g. W₂=weight of sample after drying, g. Determination of Drying efficiency:- Drying efficiency % ( ) Where, W= mass of moisture evaporated (kg) in time ‘t’ ∆H₁= Latent heat of evaporation (kJ/kg) Ic = Isolations on collector surface (kW/m2) Ac = Collector area, m2 RESULT AND DISCUSSION Evaluation of Solar Tunnel Dryer for No load condition Evaluation and testing of the Solar Tunnel Dryer was carried out under no load conditions. Fig. 5 Variation of Temperature, Humidity and Solar Radiation with Time at No load condition It was observed that the minimum inside temperature was 25.70C at 8:00 am and also observed that the minimum and maximum dryer humidity was 20 % and 32% from 08:00 am to 5:00 pm respectively. The minimum and maximum base temperature is 25.70C at 08:00 am and 63.20C at 1:30 pm respectively. The minimum solar radiation was observed at 08:00 am and maximum at 1:00 pm were 189 and 1008 W/m2 respectively. Fig. 5 clearly explains the minimum and maximum temperature of dryer, ambient temp, humidity, solar radiation. It was observed that the minimum and maximum ambient temperature of air was observed at 8:00 am and 01:30 pm that is 25.00C and 36.20C respectively. Fig. 6 Variation of Air Flow Velocity with Time at No load condition Fig. 6 shows that the variation of air flow velocity of wind velocity with respect to time. The minimum & maximum air flow velocity was observed at 09:00 am and 01:30 pm, 0.03 m/s and 2.25 m/s respectively. 0 500 1000 1500 0 20 40 60 80 8:00 10:00AM 12:l00… 2:00PM 4:00PM SolarRadiations Temperature&RH Time Ambie nt Temp. T1 ( Top ) 0 1 2 3 8:00AM 9:00AM 10:00AM 11:00AM 12:00Noon 1:00PM 2:00PM 3:00PM 4:00PM 5:00PM AirandWindVelocity Time Air and wind velocity Air and wind velocity Set Temperature If Temperature ˃ Set Temperature FAN is ON FAN is OFF Yes No
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1647 Evaluation of Solar Tunnel Dryer for Sapota Evaluation and testing of the Solar Tunnel Dryer was carried out under load conditions for drying of sapota slices. Fig. 7 Variation of Temperature, Humidity and Solar Radiation with Time at 1st Day On the first day of drying it was observed that the minimum inside temperature was 27.80C at 8:00 am. It also observed that the minimum and maximum dryer humidity was 20 % and 32 % from 08:00 am to 5:00 pm respectively. The minimum and maximum base temperature is 29.20C at 08:00 am and 52.640C at 12:00 noon. The minimum solar radiation was observed at 08:00 am and maximum at 12:00 noon were 169 and 995 W/m2 respectively. Fig. 7 clearly explains the minimum and maximum temperature of dryer, ambient temp, humidity, solar radiation. It was observed that the minimum and maximum ambient temperature of air was observed at 8:00 am and 01:30 pm that is 25.20C and 34.10C respectively. Fig. 8 Variation of Air Flow Velocity with Time at 1st Day Fig. 8 shows that the variation of air flow velocity of wind velocity with respect to time. The minimum and maximum air flow velocity was observed at 09:00 am and 03:00 pm i.e. 0.03 m/s and 1.44 m/s respectively. Fig. 9 Variation of Temperature, Humidity and Solar Radiation with Time at 2nd Day On the second day of drying it was observed that the minimum inside temperature was 29.40C at 8:00 am and also observed that the minimum and maximum dryer humidity was 20 % and 32 % from 08:00 am to 5:00 pm respectively. The minimum and maximum base temperature is 30.20C at 08:00 am and 51.170C at 12:00 noon. The minimum solar radiation was observed at 08:00 am and maximum at 12:30 noon were 153 W/m2 and 1019 W/m2 respectively. Fig. 9 shows the minimum and maximum temperature of dryer, ambient temp, humidity, solar radiation. It was observed that the minimum and maximum ambient temperature of air was observed at 8:00 am and 1:30 pm i.e. 25.20C and 38.50C respectively. Fig. 10 Variation of Air Flow Velocity with Time at 2nd Day Fig. 10 shows that the variation of air flow velocity of wind velocity with respect to time. The minimum and maximum air flow velocity was observed at 03:00 pm and 10:00 am i.e. 0.03 m/s and 1.17 m/s respectively. 0 500 1000 1500 0 20 40 60 8:00AM 10:00AM 12:00… 2:00PM 4:00PM Solar Radiation(W/mˆ2 ) Temperature(◦C) &RH(%) Time(hr) Ambien t Temp. T1 (top) 0 1 2 8:00AM 9:30AM 11:00AM 12:30PM 2:00PM 3:30PM 5:00PM Airandwind velocity(m/s) Time(hr) Air and wind… 0 1 2 Airandwind velocity(m… Time(hr) Air and wind… 0 200 400 600 800 1000 1200 0 10 20 30 40 50 60 8:00AM 10:00AM 12:00Noon 2:00PM 4:00PM SolarRadiation(W/mˆ2) Temperature(◦C)&RH(%) Time (hr) Ambie nt Temp. T1 (top) T2 (middl e)
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1648 Fig. 11: Sapota slices before drying Fig. 12: Sapota slices after drying Determination of Moisture Content Table 11: Initial Moisture Content Weigh t of empty box gm Weight of empty box + Weight of sample before oven drying (W2) gm Weight of empty box + Weight of sample after oven drying (W3) gm Moistu re conten t % (wet basis) 59.3 64.16 60.6 73.25 Table 12: Moisture Content after 1st Day Weight of empty box gm Weight of empty box + Weight of sample before oven drying (W2) gm Weight of empty box + Weight of sample after oven drying (W3) gm Moisture content % (wet basis) 59.3 63.52 62.39 26.72 Table 13: Moisture Content after 2nd Day Weight of empty box gm Weight of empty box + Weight of sample before oven drying (W2) gm Weight of empty box + Weight of sample after oven drying (W3) gm Moisture content % (wet basis) 59.3 63.69 63.24 10.22 Fig. 13: Removal of moisture from sapota per day From the fig. 13 it is observed that sapota require 2 days for drying. The drying rate is high. It is found that the initial moisture content of Sapota Slices was 73.25% which was reduced to 26.72 % on first day and on next day it was reduced to 10.22%. CONCLUSION Using the concept of basic solar conduction dryer and implementing the automation and design enhancement, the efficiency of the system and quality of agro products has been increased. By utilizing large amount of solar heat to maintain the quality of the food products is also achieved. From the experiment performed, the dryer accomplishes the temperature control at desired temperature. The overall reading observed that the maximum inside temperature was 520C. Corresponding average ambient temperature was 32.520C. It was also observed that the average solar radiation was 787.52 W/m2, average humidity was 20 % and average the air flow velocity was 0.89 m/s. The initial moisture content of Sapota slices was 73.25% which was reduced to 26.72% in 1 day and on next day it was reduced to 10.22%. REFERENCES 1. Bagh, S., Shrivastava, A., Singh, A. V., Shrivastava, A. C., Gupta L., 2015. Review on Design of temperature controlled solar dryer. International Journal of Advanced Research in Electrical, Electronics and Instrumentation Engineering, 4(11):8731-8740 2. Dangi, N., 2017. Review on Monitoring environmental parameters: humidity and 0 10 20 30 40 50 60 70 80 Initial Day 1 Day 2 Moisture Content Moisture Content
  • 7. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1649 temperature using Arduino based microcontroller and sensors. 3. Gupta, S. V., Patil, B. N., 2014. Connective drying of osmo-dehydrated sapota slices. International journal of agriculture and food science technology, 5(2); 219-226. 4. Hegde, V. N., Hosur, V. S., Rathod, S. K., Harsoor, P. A. and Badari, N., 2015. Review on Design, fabrication and performance evaluation of solar dryer for banana. Energy, Sustainability and Society Journal. 5. Louis, L. 2016. Review on Working principle of Arduino and using it as a tool for study and research, International Journal of Control, Automation, Communication and System (IJCACS), 1(2):21-29. 6. Moloney, C., 2016. India's major agricultural produce losses. [Online]. Available: https://www.firstpost.com/business/indias-major- agricultural-produce-losses-es timated-at-rs- 92000-cr-2949002.html [Accessed on 30-July-2018] 7. Singh, D., Meena, M. L., Chaudhary, M., Dayal, H. and Dudi, A., K., 2004. Review on Local Solar Tunnel Dryer for Small Scale, Entrepreneurship in Rural India, Central Arid, Zone Research Institute, Pali, Rajasthan, India. : 10-21. 8. Vardini, P. S., Hegade, V. N., Panvare, N. L., 2016. Design and Performance Evaluation of Solar Tunnel Dryer 9(3):955-967.