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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 270
Parametric Optimization of Solar Parabolic Collectors Using AHP-
TOPSIS
J Ravi Kumar1, K Dharma reddy2, P Venkataramaiah3
1PG Scholar, Dept. of Mechanical Engineering, Sri Venkateswara University, Tirupati, A.P., India.
2Assistant Professor, Dept. of Mechanical Engineering, Sri Venkateswara University, Tirupati, A.P., India.
3Professor, Dept. of Mechanical Engineering, Sri Venkateswara University, Tirupati, A.P., India.
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract - In the present work the behavior of linear solar
parabolic Collector is studied. An experimental design is
prepared based on the considered parabolic collector
parameters such as Temperature, DischargeandPeriodof Sun
Incidence (POI). The copper alloy c101 tube and aluminum
alloy 1199 are used in experimental setup as absorbers.
Copper alloy c101 tube has composition of Copper(99.998%),
Antimony (0.1ppm), Arsenic(0.1ppm), Bisumasu (0.1ppm),
Cadmium (<0.1ppm), Iron (1ppm), Lead (1ppm), Manganese
(<=0.1ppm), Nickel (0.5ppm) and Aluminium alloy1199 has
aluminium (99.98%), copper(0.006%), gallium(0.005%), iron
(0.005%), titanium(0.002%), magnesium (0.006%) and the
reflective surfaces are considered at two levels, one is Glass
mirror and other is polished aluminum. Present work is
focused on improvement of temperature of working fluid
(water) and discharge of fluid, which influenced by
parameters such as absorber tube materials, reflective sheet
materials, time duration. The experiments are conducted
according to the Taguchi design on the solar parabolic
collector. This data is analyzedusingAHP-TOPSISandoptimal
parameter combination has been identified.
Key Words: 1)Parabolic Shaped Structure, 2)
Supporting legs, 3) Reflective Surfaces, 4) Heat
collecting element(Absorber), 5) Auto Tracking
System, 6) Piping system and Storage tank.
1. INTRODUCTION
The powerful presence of the sun is hard to ignore in one’s
everyday life: indeed, the majority of life on Earth could not
exist without its vast output of radiant energy. At any given
moment, the Earth’s upper atmosphere receives solar
radiation amounting to 174 PW (Peta Watts) of power. As
shown in Figure 1.2, about 55% of this reaches the Earth’s
surface and is either absorbed or reflected by land and
oceans. With such a vast amount of solar energy available,
humanity could meet its demands by harnessing just a small
fraction of this. Indeed, the total annualsolarradiationfalling
on the Earth is more than 7500 times greater than the
world’s total annual primary energy consumption (WEC
2007). Furthermore, unlike fossil fuels, solar energy will
continue to be available for billions of years.
1.1 Introduction of Solar Thermal systems
Concentrating solar technologies,such as the parabolicdish,
compound parabolic collector and parabolic trough can
operate at high temperatures and are used to supply
industrial process heat, off-grid electricityandbulkelectrical
power. In a parabolic trough solar collector, or PTSC, the
reflective profile focuses sunlight on a linear heat collecting
element (HCE) throughwhichaheattransferfluidispumped.
The fluid captures solar energy in the form of heat that can
then be used in a variety of applications.
1.2 Experimental Setup
(a) The experimental setup consists of the following
components:
1)Parabolic Shaped Structure, 2) Supporting legs, 3)
Reflective Surfaces, 4) Heat collectingelement(Absorber), 5)
Auto Tracking System, 6) Piping system and Storage tank.
The whole experimental setup is placed on the top of the
buildings. All the components are assembled to form the
entire setup. The entire set is placed in the N_S direction to
face the axis of the parabolic trough towards east.
(b) Plan of investigation: It is planned that the
experiments are conducted according to the L36 array with
respect of factors and levels of problem.
Table2.: Process parameters and their levels
S.
No
Process
Parameters
Level 1 Level 1 Level 1
1 Reflectivity Polished
Aluminum
(AP)
Glass
Mirror
(GM)
-
2 Absorptivity Copper
Alloy
C101 tube
Aluminum
Alloy
1199 tube
-
3 Period of
sun
incidence
(POI)
10.00AM-
12.00PM
12.00PM-
2.00PM
2.00PM-
4.00PM
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 271
Fig-1.Experimental Setup
2. EXPERIMENTAL WORK
The experiments were conducted for several days on the
solar parabolic trough by changing the reflective and
absorber materials. After absorbing sufficient radiation, the
water in the absorber tube gets heated and its density
decreases. Due to the differential,and theendoftheabsorber
tube is closed the natural convection in counter flow
direction hasoccurred.ateachexperimentthetemperatureis
noted at the surface of the absorber and bottom of the water
tank ,the water in storage tank is heated by the natural
convection.
Table2.1: Experimental results and response data
POI Absor
-ber
Tube
Refle
-ctor
Output
Temp
(°C)
Dischar
-ge
(lit/hr)
Thermal
efficiency
(%)
10 a.m-
12p.m
Cu
alloy
GM 60.6 19 89.37
12a.m-
2p.m
Cu
alloy
GM 75.3 16 135
2p.m-
4p.m
Cu
alloy
GM 68.1 18.5 112.5
10a.m-
12p.m
Cu
alloy
GM 61.3 18.3 91.6
12p.m-
2p.m
Cu
alloy
GM 78.5 15 145
2p.m-
4p.m
Cu
alloy
GM 65.5 17 104.68
10a.m-
12p.m
Cu
alloy
GM 59 19.1 84.37
12p.m-
2p.m
Cu
alloy
GM 77 15.5 140.6
2p.m-
4p.m
Cu
alloy
GM 65.2 18 103.7
10a.m-
12p.m
Cu
alloy
Al
Sheet
51 19.4 59.37
12p.m-
2p.m
Cu
alloy
Al
Sheet
65.3 18.7 104.06
2p.m-
4p.m
Cu
alloy
Al
Sheet
58.1 19.1 81.56
10a.m-
12p.m
Cu
alloy
Al
Sheet
50.4 19 57.5
12p.m-
2p.m
Cu
alloy
Al
Sheet
62.2 18.8 94.37
2p.m-
4p.m
Cu
alloy
Al
Sheet
56.1 17.2 75.31
10a.m-
12p.m
Cu
alloy
Al
Sheet
49.3 19.2 54.06
12p.m-
2p.m
Cu
alloy
Al
Sheet
66 18.4 106.25
2p.m-
4p.m
Cu
alloy
Al
Sheet 59.2 18.6 85
10a.m-
12p.m
Al
alloy
GM 50 19.3 56.25
12p.m-
2p.m
Al
alloy
GM 68.2 18.5 113.12
2p.m-
4p.m
Al
alloy
GM 59.2 19 85
10a.m-
12p.m
Al
alloy
GM 49.2 19.1 54.06
12p.m-
2p.m
Al
alloy
GM 67.5 18.7 110.09
2p.m-
4p.m
Al
alloy
GM 58.2 19 81.8
10a.m-
12p.m
Al
alloy
GM 51.2 19.2 60
12p.m-
2p.m
Al
alloy
GM 69.3 18 116.56
2p.m-
4p.m
Al
alloy
GM 59.4 18.7 85
10a.m-
12p.m
Al
alloy
Al
Sheet
46.2 19.6 44.37
12p.m-
2p.m
Al
alloy
Al
Sheet
58.1 19.1 81.56
2p.m-
4p.m
Al
alloy
Al
Sheet
49.2 19.4 53.7
10a.m-
12p.m
Al
alloy
Al
Sheet
45.4 19.7 41.87
12p.m-
2p.m
Al
alloy
Al
Sheet
57.6 19 80
2p.m-
4p.m
Al
alloy
Al
Sheet
48.2 19.6 56
10a.m-
12p.m
Al
alloy
Al
Sheet
43.3 19.8 35.31
12p.m-
2p.m
Al
alloy
Al
Sheet
55.2 19.2 72.5
2p.m-
4p.m
Al
alloy
Al
Sheet
46.5 19.4 45.31
3. EVALUATION OF WEIGHTAGE FOR RESPONSES
USING IN AHP
AHP method is used to evaluatetheweightagesforresponses
using the procedure given in section
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 272
Step I
Specify the set of criteria for evaluating the weights and
tabulated in Table3.1
Temperature Efficiency Discharge
Temperature EP Not
BEtMP
Not MP
Efficiency BEtMP EP Not
BEtMP
Discharge MP BEtMP EP
Step II
The criterion is compared with each other in order to
determine the relative importance of each factor to
accomplish the overall objective. The importance of each
factor is represented on the left (row) relative to the
importance of the factor on top (column) of the matrix.
Thereby, consider the higher value which means the factors
on the left is relatively more important than the factor on the
top and compute the priorities or weights of the criteria
based on this information and is tabulated as in Table
Table3.2: Pair wise comparison matrix
Tem
p
Therma
-l
Efficien
cy
Discha
r-ge
Eigen
Value
s
(EV)
Weighta
g-es
(EV/3.36
7)
Temp 1 1/2 1/3 0.550
2
0.1633
Efficien
cy
2 1 1/2 1 0.2969
Dischar
ge
3 2 1 1.817
1
0.5396
Total 6 3.5 1.83 3.367
3
λmax 3.007
Step III
Compute Eigen vectors for each matrix by approximation
of priorities using geometric mean method. This is done by
multiplying the elements in each row and taking their nth
root and these valuesare shown below.Wherenisnumberof
criteria.
 Eigen vector or value for Temperature
EVtemp=
 For Efficiency
EV Effi=
 For Discharge
EV Dis=
Step IV
Sum ofeachcolumnisthenmultipliedwithcorresponding
Priority vector. Sum of column one with Priority vector of
component one and so on and sum of product is called
Principal Eigen vector.
λ max = *Pvi
λ max = 3.006
Step V
Consistency index is calculated using the equation C. I =
(λmax - n)/n – 1
C.I= (λmax-n)/(n-1) = (3.006-3)/3-1 = 0.0032
Then calculation of consistency ratio (CR)
In this case R.I is 0.58 as the size of matrix is three (Table
4.2). The value of CR should be around 10% to be acceptable.
C.R = (C.I/R.I) = (0.0032 /0.58) = 0.055
Hence the C.R is less than 10%; therefore the pair wise
comparison matrix is acceptable and the weightageobtained
for output responses as follows.
Weightages:
Temperature =0.1633
Thermal Efficiency =0.2969
Discharge =0.5396
4. SELECTION OF OPTIMAL PROCESS PARAMETERS
COMBINATION USING TOPSIS METHOD
TOPSIS method is used to determine the optimum
parameter combination by analyzing the experimental data.
Step1: The first step is to formulate decision matrix with
‘m’ alternatives and ‘n’ attributes are shown in table 3.1.
Step 2: Take weightages for each response, after
normalization ofexperimentaldata,theweightednormalized
decision matrix is obtained by using equation (2). This
weighted normalizedmatrixisformedbyintegratingtheAHP
weightage calculated in table 4.2 with TOPSIS normalization
matrix
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 273
rij= ………………………………….(1)
𝑉𝑖𝑗 = 𝑊𝑖 × 𝑟𝑖𝑗……………………………….…….(2)
Si
+ = ……………… (3)
Si
- = ……………..… (4)
Table4.1: Normalization Matrix
Step 4: After obtaining weighted normalizedmatrix,Positive
separation ideal solution (PIS) and negativeseparationideal
solution (NIS) are determined. Using Equations 3 and 4.
These ideal solutions are as follows.
From weighted normalized decision-making matrix, the
positive separation ideal solution V+ obtained as
V+= {0.036, 0.052, 0.143}
From weighted normalized decision-making matrix, the
negative separation ideal solution V-obtained as
V-= {0.019, 0.039, 0.036}
Step 5: The separation of each alternative from positives
separation ideal solution (PSIS) and negative separation
NORMALISATION MATRIX
s.no Output
Temp
Discharge Efficiency
1 0.1702 0.1701 0.1695
2 0.2116 0.1432 0.2561
3 0.1913 0.1655 0.2134
4 0.1722 0.1638 0.1738
5 0.2205 0.1342 0.2751
6 0.1840 0.1521 0.1986
7 0.1658 0.1709 0.1601
8 0.2163 0.1387 0.2657
9 0.1832 0.1611 0.1967
10 0.1433 0.1736 0.1126
11 0.1835 0.1673 0.1974
12 0.1632 0.1709 0.1547
13 0.1416 0.17007 0.1091
14 0.1747 0.1682 0.1791
15 0.1576 0.1539 0.1429
16 0.1385 0.1718 0.1025
17 0.1854 0.1647 0.2016
18 0.1663 0.1664 0.1612
19 0.1405 0.1727 0.1067
20 0.1916 0.1655 0.2146
21 0.1663 0.17007 0.1612
22 0.1382 0.1709 0.1025
23 0.1896 0.1673 0.2088
24 0.1635 0.17007 0.1552
25 0.1438 0.1718 0.1138
26 0.1947 0.1611 0.2211
27 0.1669 0.1673 0.1612
28 0.1298 0.1754 0.0841
29 0.1632 0.1709 0.1547
30 0.1382 0.1736 0.1018
31 0.1275 0.1763 0.0794
32 0.1618 0.17007 0.1518
33 0.1354 0.1754 0.1062
34 0.1216 0.1772 0.0670
35 0.1551 0.1718 0.1375
36 0.1306 0.1736 0.0859
WEIGHTED NORMALSED MATRIX
s.no Output
Temp
Discharg
e
Efficienc
y
1 0.027 0.051 0.091
2 0.034 0.042 0.138
3 0.031 0.049 0.115
4 0.028 0.048 0.093
5 0.036 0.039 0.148
6 0.031 0.045 0.107
7 0.027 0.051 0.086
8 0.035 0.041 0.143
9 0.029 0.047 0.106
10 0.023 0.051 0.061
11 0.029 0.049 0.106
12 0.026 0.051 0.083
13 0.023 0.051 0.058
14 0.028 0.049 0.096
15 0.025 0.045 0.077
16 0.022 0.051 0.055
17 0.031 0.048 0.108
18 0.027 0.049 0.087
19 0.022 0.051 0.057
20 0.031 0.049 0.115
21 0.027 0.051 0.087
22 0.022 0.051 0.055
23 0.030 0.049 0.112
24 0.026 0.051 0.083
25 0.023 0.051 0.061
26 0.031 0.047 0.119
27 0.027 0.049 0.087
28 0.021 0.052 0.045
29 0.026 0.050 0.083
30 0.022 0.051 0.054
31 0.020 0.052 0.042
32 0.026 0.050 0.081
33 0.022 0.052 0.057
34 0.019 0.052 0.036
35 0.025 0.051 0.074
36 0.021 0.051 0.046
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 274
ideal solution (NSIS) are calculated using the equation as in
the Table 4.3
Table 4.3: Positive and Negative Separation ideal solution
Step 6: The closeness co-efficient (Table 4.4) of each
alternative is CCi =
Table 4.4: Closeness coefficient
Step 7: Rank the preference order based on their largest
relative closeness co-efficient. It is observed from the
Table 4.4, for the higher closeness coefficient is obtained
for 8th experimental run. Hence the best parameter
combinations of experimental 8th run are in the following.
Best combination of parameter
 Period of incidence : 12.00 p.m. – 2.00 p.m.
 Absorber Tube : Copper alloy c101
 Reflector : Glass Mirror
Best Output Responses for best combination of
reflector and absorber tube
 Temperature : 77°C
 Discharge : 15.5 lit/hr.
 Thermal Efficiency : 140.6%
s.no Si
+ Si
-
1 0.052 0.056
2 0.011 0.103
3 0.028 0.081
4 0.051 0.058
5 0.013 0.113
6 0.037 0.072
7 0.057 0.051
8 0.011 0.108
9 0.038 0.07
10 0.083 0.027
11 0.037 0.071
12 0.061 0.049
13 0.085 0.025
14 0.047 0.061
15 0.067 0.041
16 0.089 0.022
17 0.035 0.074
18 0.057 0.052
19 0.086 0.024
20 0.028 0.081
21 0.057 0.052
22 0.089 0.022
23 0.031 0.078
24 0.061 0.049
25 0.082 0.027
26 0.024 0.084
27 0.057 0.052
28 0.099 0.015
29 0.061 0.049
30 0.089 0.022
31 0.102 0.014
32 0.062 0.047
33 0.087 0.024
34 0.108 0.012
35 0.071 0.041
36 0.098 0.015
s.no CCI RANK
1 0.521 14
2 0.901 2
3 0.736 6
4 0.539 13
5 0.892 3
6 0.657 9
7 0.473 18
8 0.904 1
9 0.652 11
10 0.248 26
11 0.657 10
12 0.447 20
13 0.228 27
14 0.566 12
15 0.382 23
16 0.201 30
17 0.677 8
18 0.478 17
19 0.221 28
20 0.742 5
21 0.479 15
22 0.201 31
23 0.714 7
24 0.449 19
25 0.252 25
26 0.772 4
27 0.478 16
28 0.135 34
29 0.447 21
30 0.201 32
31 0.123 35
32 0.432 22
33 0.221 29
34 0.105 36
35 0.364 24
36 0.137 32
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056
Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072
© 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 275
Conclusions
The following conclusions are drawn from the results.
 In the present work, the behaviour of linear solar
parabolic Collector for cooking system is studied
and analysed using Mathematical models.
 Finally experimental response data is analysed
using AHP-TOPSIS and optimum parameters
levels have been identified.
 Among the combination of different reflector and
absorber, glass mirror and copper alloy c101 tube
combination is given best results for obtaining
maximum temperature and discharge, thermal
efficiency.
References
[1] A. Kahrobaian and H. Malekmohammadi (2008):
Energy optimization Applied to Linear Parabolic
Solar collectors. Journal of faculty of engineering,
Vol.42.No.1 2008 PP-131-144
[2] Aneirson Francisco and da silva (2013): Multi-choice
mixed integer goal programming optimization for real
problems in a sugar and ethanol milling company,
Applied Mathematical Modeling, 37(2013) 6146-6162.
[3] Delfin Silio Salcines, Carlos Renedo Estebanez (2009):
Simulation of solar domestic water heating system,
with different collector efficiencies and different
volume storage tanks.
[4] Fernandez-Garcia, E.Zarza (2010) “Parabolic solar
through collectors and their applications” Elsevier
journal of Renewable energy, Vol.14, pp.1695–1721
[5] Sairam, P. Mohan Reddy and P. Venkataramaiah
(2012): Optimization of a solar parabolic in winter
using Grey-Taguchi approach: International Journal of
Engineering Research and Applications (IJERA). ISSN:
2248-9622, Vol.2, Issue 1, Jan-Feb 2012, PP. 816-824

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Parametric Optimization of Solar Parabolic Collectors Using AHP-TOPSIS

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 270 Parametric Optimization of Solar Parabolic Collectors Using AHP- TOPSIS J Ravi Kumar1, K Dharma reddy2, P Venkataramaiah3 1PG Scholar, Dept. of Mechanical Engineering, Sri Venkateswara University, Tirupati, A.P., India. 2Assistant Professor, Dept. of Mechanical Engineering, Sri Venkateswara University, Tirupati, A.P., India. 3Professor, Dept. of Mechanical Engineering, Sri Venkateswara University, Tirupati, A.P., India. ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - In the present work the behavior of linear solar parabolic Collector is studied. An experimental design is prepared based on the considered parabolic collector parameters such as Temperature, DischargeandPeriodof Sun Incidence (POI). The copper alloy c101 tube and aluminum alloy 1199 are used in experimental setup as absorbers. Copper alloy c101 tube has composition of Copper(99.998%), Antimony (0.1ppm), Arsenic(0.1ppm), Bisumasu (0.1ppm), Cadmium (<0.1ppm), Iron (1ppm), Lead (1ppm), Manganese (<=0.1ppm), Nickel (0.5ppm) and Aluminium alloy1199 has aluminium (99.98%), copper(0.006%), gallium(0.005%), iron (0.005%), titanium(0.002%), magnesium (0.006%) and the reflective surfaces are considered at two levels, one is Glass mirror and other is polished aluminum. Present work is focused on improvement of temperature of working fluid (water) and discharge of fluid, which influenced by parameters such as absorber tube materials, reflective sheet materials, time duration. The experiments are conducted according to the Taguchi design on the solar parabolic collector. This data is analyzedusingAHP-TOPSISandoptimal parameter combination has been identified. Key Words: 1)Parabolic Shaped Structure, 2) Supporting legs, 3) Reflective Surfaces, 4) Heat collecting element(Absorber), 5) Auto Tracking System, 6) Piping system and Storage tank. 1. INTRODUCTION The powerful presence of the sun is hard to ignore in one’s everyday life: indeed, the majority of life on Earth could not exist without its vast output of radiant energy. At any given moment, the Earth’s upper atmosphere receives solar radiation amounting to 174 PW (Peta Watts) of power. As shown in Figure 1.2, about 55% of this reaches the Earth’s surface and is either absorbed or reflected by land and oceans. With such a vast amount of solar energy available, humanity could meet its demands by harnessing just a small fraction of this. Indeed, the total annualsolarradiationfalling on the Earth is more than 7500 times greater than the world’s total annual primary energy consumption (WEC 2007). Furthermore, unlike fossil fuels, solar energy will continue to be available for billions of years. 1.1 Introduction of Solar Thermal systems Concentrating solar technologies,such as the parabolicdish, compound parabolic collector and parabolic trough can operate at high temperatures and are used to supply industrial process heat, off-grid electricityandbulkelectrical power. In a parabolic trough solar collector, or PTSC, the reflective profile focuses sunlight on a linear heat collecting element (HCE) throughwhichaheattransferfluidispumped. The fluid captures solar energy in the form of heat that can then be used in a variety of applications. 1.2 Experimental Setup (a) The experimental setup consists of the following components: 1)Parabolic Shaped Structure, 2) Supporting legs, 3) Reflective Surfaces, 4) Heat collectingelement(Absorber), 5) Auto Tracking System, 6) Piping system and Storage tank. The whole experimental setup is placed on the top of the buildings. All the components are assembled to form the entire setup. The entire set is placed in the N_S direction to face the axis of the parabolic trough towards east. (b) Plan of investigation: It is planned that the experiments are conducted according to the L36 array with respect of factors and levels of problem. Table2.: Process parameters and their levels S. No Process Parameters Level 1 Level 1 Level 1 1 Reflectivity Polished Aluminum (AP) Glass Mirror (GM) - 2 Absorptivity Copper Alloy C101 tube Aluminum Alloy 1199 tube - 3 Period of sun incidence (POI) 10.00AM- 12.00PM 12.00PM- 2.00PM 2.00PM- 4.00PM
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 271 Fig-1.Experimental Setup 2. EXPERIMENTAL WORK The experiments were conducted for several days on the solar parabolic trough by changing the reflective and absorber materials. After absorbing sufficient radiation, the water in the absorber tube gets heated and its density decreases. Due to the differential,and theendoftheabsorber tube is closed the natural convection in counter flow direction hasoccurred.ateachexperimentthetemperatureis noted at the surface of the absorber and bottom of the water tank ,the water in storage tank is heated by the natural convection. Table2.1: Experimental results and response data POI Absor -ber Tube Refle -ctor Output Temp (°C) Dischar -ge (lit/hr) Thermal efficiency (%) 10 a.m- 12p.m Cu alloy GM 60.6 19 89.37 12a.m- 2p.m Cu alloy GM 75.3 16 135 2p.m- 4p.m Cu alloy GM 68.1 18.5 112.5 10a.m- 12p.m Cu alloy GM 61.3 18.3 91.6 12p.m- 2p.m Cu alloy GM 78.5 15 145 2p.m- 4p.m Cu alloy GM 65.5 17 104.68 10a.m- 12p.m Cu alloy GM 59 19.1 84.37 12p.m- 2p.m Cu alloy GM 77 15.5 140.6 2p.m- 4p.m Cu alloy GM 65.2 18 103.7 10a.m- 12p.m Cu alloy Al Sheet 51 19.4 59.37 12p.m- 2p.m Cu alloy Al Sheet 65.3 18.7 104.06 2p.m- 4p.m Cu alloy Al Sheet 58.1 19.1 81.56 10a.m- 12p.m Cu alloy Al Sheet 50.4 19 57.5 12p.m- 2p.m Cu alloy Al Sheet 62.2 18.8 94.37 2p.m- 4p.m Cu alloy Al Sheet 56.1 17.2 75.31 10a.m- 12p.m Cu alloy Al Sheet 49.3 19.2 54.06 12p.m- 2p.m Cu alloy Al Sheet 66 18.4 106.25 2p.m- 4p.m Cu alloy Al Sheet 59.2 18.6 85 10a.m- 12p.m Al alloy GM 50 19.3 56.25 12p.m- 2p.m Al alloy GM 68.2 18.5 113.12 2p.m- 4p.m Al alloy GM 59.2 19 85 10a.m- 12p.m Al alloy GM 49.2 19.1 54.06 12p.m- 2p.m Al alloy GM 67.5 18.7 110.09 2p.m- 4p.m Al alloy GM 58.2 19 81.8 10a.m- 12p.m Al alloy GM 51.2 19.2 60 12p.m- 2p.m Al alloy GM 69.3 18 116.56 2p.m- 4p.m Al alloy GM 59.4 18.7 85 10a.m- 12p.m Al alloy Al Sheet 46.2 19.6 44.37 12p.m- 2p.m Al alloy Al Sheet 58.1 19.1 81.56 2p.m- 4p.m Al alloy Al Sheet 49.2 19.4 53.7 10a.m- 12p.m Al alloy Al Sheet 45.4 19.7 41.87 12p.m- 2p.m Al alloy Al Sheet 57.6 19 80 2p.m- 4p.m Al alloy Al Sheet 48.2 19.6 56 10a.m- 12p.m Al alloy Al Sheet 43.3 19.8 35.31 12p.m- 2p.m Al alloy Al Sheet 55.2 19.2 72.5 2p.m- 4p.m Al alloy Al Sheet 46.5 19.4 45.31 3. EVALUATION OF WEIGHTAGE FOR RESPONSES USING IN AHP AHP method is used to evaluatetheweightagesforresponses using the procedure given in section
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 272 Step I Specify the set of criteria for evaluating the weights and tabulated in Table3.1 Temperature Efficiency Discharge Temperature EP Not BEtMP Not MP Efficiency BEtMP EP Not BEtMP Discharge MP BEtMP EP Step II The criterion is compared with each other in order to determine the relative importance of each factor to accomplish the overall objective. The importance of each factor is represented on the left (row) relative to the importance of the factor on top (column) of the matrix. Thereby, consider the higher value which means the factors on the left is relatively more important than the factor on the top and compute the priorities or weights of the criteria based on this information and is tabulated as in Table Table3.2: Pair wise comparison matrix Tem p Therma -l Efficien cy Discha r-ge Eigen Value s (EV) Weighta g-es (EV/3.36 7) Temp 1 1/2 1/3 0.550 2 0.1633 Efficien cy 2 1 1/2 1 0.2969 Dischar ge 3 2 1 1.817 1 0.5396 Total 6 3.5 1.83 3.367 3 λmax 3.007 Step III Compute Eigen vectors for each matrix by approximation of priorities using geometric mean method. This is done by multiplying the elements in each row and taking their nth root and these valuesare shown below.Wherenisnumberof criteria.  Eigen vector or value for Temperature EVtemp=  For Efficiency EV Effi=  For Discharge EV Dis= Step IV Sum ofeachcolumnisthenmultipliedwithcorresponding Priority vector. Sum of column one with Priority vector of component one and so on and sum of product is called Principal Eigen vector. λ max = *Pvi λ max = 3.006 Step V Consistency index is calculated using the equation C. I = (λmax - n)/n – 1 C.I= (λmax-n)/(n-1) = (3.006-3)/3-1 = 0.0032 Then calculation of consistency ratio (CR) In this case R.I is 0.58 as the size of matrix is three (Table 4.2). The value of CR should be around 10% to be acceptable. C.R = (C.I/R.I) = (0.0032 /0.58) = 0.055 Hence the C.R is less than 10%; therefore the pair wise comparison matrix is acceptable and the weightageobtained for output responses as follows. Weightages: Temperature =0.1633 Thermal Efficiency =0.2969 Discharge =0.5396 4. SELECTION OF OPTIMAL PROCESS PARAMETERS COMBINATION USING TOPSIS METHOD TOPSIS method is used to determine the optimum parameter combination by analyzing the experimental data. Step1: The first step is to formulate decision matrix with ‘m’ alternatives and ‘n’ attributes are shown in table 3.1. Step 2: Take weightages for each response, after normalization ofexperimentaldata,theweightednormalized decision matrix is obtained by using equation (2). This weighted normalizedmatrixisformedbyintegratingtheAHP weightage calculated in table 4.2 with TOPSIS normalization matrix
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 273 rij= ………………………………….(1) 𝑉𝑖𝑗 = 𝑊𝑖 × 𝑟𝑖𝑗……………………………….…….(2) Si + = ……………… (3) Si - = ……………..… (4) Table4.1: Normalization Matrix Step 4: After obtaining weighted normalizedmatrix,Positive separation ideal solution (PIS) and negativeseparationideal solution (NIS) are determined. Using Equations 3 and 4. These ideal solutions are as follows. From weighted normalized decision-making matrix, the positive separation ideal solution V+ obtained as V+= {0.036, 0.052, 0.143} From weighted normalized decision-making matrix, the negative separation ideal solution V-obtained as V-= {0.019, 0.039, 0.036} Step 5: The separation of each alternative from positives separation ideal solution (PSIS) and negative separation NORMALISATION MATRIX s.no Output Temp Discharge Efficiency 1 0.1702 0.1701 0.1695 2 0.2116 0.1432 0.2561 3 0.1913 0.1655 0.2134 4 0.1722 0.1638 0.1738 5 0.2205 0.1342 0.2751 6 0.1840 0.1521 0.1986 7 0.1658 0.1709 0.1601 8 0.2163 0.1387 0.2657 9 0.1832 0.1611 0.1967 10 0.1433 0.1736 0.1126 11 0.1835 0.1673 0.1974 12 0.1632 0.1709 0.1547 13 0.1416 0.17007 0.1091 14 0.1747 0.1682 0.1791 15 0.1576 0.1539 0.1429 16 0.1385 0.1718 0.1025 17 0.1854 0.1647 0.2016 18 0.1663 0.1664 0.1612 19 0.1405 0.1727 0.1067 20 0.1916 0.1655 0.2146 21 0.1663 0.17007 0.1612 22 0.1382 0.1709 0.1025 23 0.1896 0.1673 0.2088 24 0.1635 0.17007 0.1552 25 0.1438 0.1718 0.1138 26 0.1947 0.1611 0.2211 27 0.1669 0.1673 0.1612 28 0.1298 0.1754 0.0841 29 0.1632 0.1709 0.1547 30 0.1382 0.1736 0.1018 31 0.1275 0.1763 0.0794 32 0.1618 0.17007 0.1518 33 0.1354 0.1754 0.1062 34 0.1216 0.1772 0.0670 35 0.1551 0.1718 0.1375 36 0.1306 0.1736 0.0859 WEIGHTED NORMALSED MATRIX s.no Output Temp Discharg e Efficienc y 1 0.027 0.051 0.091 2 0.034 0.042 0.138 3 0.031 0.049 0.115 4 0.028 0.048 0.093 5 0.036 0.039 0.148 6 0.031 0.045 0.107 7 0.027 0.051 0.086 8 0.035 0.041 0.143 9 0.029 0.047 0.106 10 0.023 0.051 0.061 11 0.029 0.049 0.106 12 0.026 0.051 0.083 13 0.023 0.051 0.058 14 0.028 0.049 0.096 15 0.025 0.045 0.077 16 0.022 0.051 0.055 17 0.031 0.048 0.108 18 0.027 0.049 0.087 19 0.022 0.051 0.057 20 0.031 0.049 0.115 21 0.027 0.051 0.087 22 0.022 0.051 0.055 23 0.030 0.049 0.112 24 0.026 0.051 0.083 25 0.023 0.051 0.061 26 0.031 0.047 0.119 27 0.027 0.049 0.087 28 0.021 0.052 0.045 29 0.026 0.050 0.083 30 0.022 0.051 0.054 31 0.020 0.052 0.042 32 0.026 0.050 0.081 33 0.022 0.052 0.057 34 0.019 0.052 0.036 35 0.025 0.051 0.074 36 0.021 0.051 0.046
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 274 ideal solution (NSIS) are calculated using the equation as in the Table 4.3 Table 4.3: Positive and Negative Separation ideal solution Step 6: The closeness co-efficient (Table 4.4) of each alternative is CCi = Table 4.4: Closeness coefficient Step 7: Rank the preference order based on their largest relative closeness co-efficient. It is observed from the Table 4.4, for the higher closeness coefficient is obtained for 8th experimental run. Hence the best parameter combinations of experimental 8th run are in the following. Best combination of parameter  Period of incidence : 12.00 p.m. – 2.00 p.m.  Absorber Tube : Copper alloy c101  Reflector : Glass Mirror Best Output Responses for best combination of reflector and absorber tube  Temperature : 77°C  Discharge : 15.5 lit/hr.  Thermal Efficiency : 140.6% s.no Si + Si - 1 0.052 0.056 2 0.011 0.103 3 0.028 0.081 4 0.051 0.058 5 0.013 0.113 6 0.037 0.072 7 0.057 0.051 8 0.011 0.108 9 0.038 0.07 10 0.083 0.027 11 0.037 0.071 12 0.061 0.049 13 0.085 0.025 14 0.047 0.061 15 0.067 0.041 16 0.089 0.022 17 0.035 0.074 18 0.057 0.052 19 0.086 0.024 20 0.028 0.081 21 0.057 0.052 22 0.089 0.022 23 0.031 0.078 24 0.061 0.049 25 0.082 0.027 26 0.024 0.084 27 0.057 0.052 28 0.099 0.015 29 0.061 0.049 30 0.089 0.022 31 0.102 0.014 32 0.062 0.047 33 0.087 0.024 34 0.108 0.012 35 0.071 0.041 36 0.098 0.015 s.no CCI RANK 1 0.521 14 2 0.901 2 3 0.736 6 4 0.539 13 5 0.892 3 6 0.657 9 7 0.473 18 8 0.904 1 9 0.652 11 10 0.248 26 11 0.657 10 12 0.447 20 13 0.228 27 14 0.566 12 15 0.382 23 16 0.201 30 17 0.677 8 18 0.478 17 19 0.221 28 20 0.742 5 21 0.479 15 22 0.201 31 23 0.714 7 24 0.449 19 25 0.252 25 26 0.772 4 27 0.478 16 28 0.135 34 29 0.447 21 30 0.201 32 31 0.123 35 32 0.432 22 33 0.221 29 34 0.105 36 35 0.364 24 36 0.137 32
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395 -0056 Volume: 04 Issue: 03 | Mar -2017 www.irjet.net p-ISSN: 2395-0072 © 2017, IRJET | Impact Factor value: 5.181 | ISO 9001:2008 Certified Journal | Page 275 Conclusions The following conclusions are drawn from the results.  In the present work, the behaviour of linear solar parabolic Collector for cooking system is studied and analysed using Mathematical models.  Finally experimental response data is analysed using AHP-TOPSIS and optimum parameters levels have been identified.  Among the combination of different reflector and absorber, glass mirror and copper alloy c101 tube combination is given best results for obtaining maximum temperature and discharge, thermal efficiency. References [1] A. Kahrobaian and H. Malekmohammadi (2008): Energy optimization Applied to Linear Parabolic Solar collectors. Journal of faculty of engineering, Vol.42.No.1 2008 PP-131-144 [2] Aneirson Francisco and da silva (2013): Multi-choice mixed integer goal programming optimization for real problems in a sugar and ethanol milling company, Applied Mathematical Modeling, 37(2013) 6146-6162. [3] Delfin Silio Salcines, Carlos Renedo Estebanez (2009): Simulation of solar domestic water heating system, with different collector efficiencies and different volume storage tanks. [4] Fernandez-Garcia, E.Zarza (2010) “Parabolic solar through collectors and their applications” Elsevier journal of Renewable energy, Vol.14, pp.1695–1721 [5] Sairam, P. Mohan Reddy and P. Venkataramaiah (2012): Optimization of a solar parabolic in winter using Grey-Taguchi approach: International Journal of Engineering Research and Applications (IJERA). ISSN: 2248-9622, Vol.2, Issue 1, Jan-Feb 2012, PP. 816-824