Experiments were carried out in three cnescutive days in May, 2022 atthe University of El Oued in Algeria. The readings were taken hourly from 7:00 a.m. to 6:00 p.m.
The effectiveness of a hemispheric solar still is influenced by solar intensity and ambient temperatures. As a result, hourly readings of the experiment's solar intensity and ambient temperature are required. During experimentation test hours, Fig. 5 depicts the variation in ambient temperatures and solar intensity. The solar intensity increases until midday on each of the three test days, then gradually decreases as time passes until reaches to lowest point of sunset. Around 1:00 p.m., the highest recorded temperature of ambient was also reached. This means test locations are subjected to the same climatic and weather conditions, they can be compared more precisely.
The performance of the hemispherical solar still (CHSWF) is compared to that of the cylindrical hemispherical solar still (CyFHS) and the conical hemispherical still (CoFHS) with fins spaced differently (3, 3.75, and 4.5 cm).
Figure 6 depicts a change in water temperature for the three distinct configurations of CyFHS and CoFHS on May 13, 14, and 15.
The maximum temperature of the water basin appears to increase as the distance between fins evolves. At about 2:00 p.m., the maximum water basin temperatures of CHSWF, CyFHS (Case 1), CoFHS (Case 1), CyFHS (Case 2), CoFHS (Case 2), CyFHS (Case 3), and CoFHS (Case 3) are 55, 58, 61, 58, 65, 65, and 67, respectively.
From 7:00 a.m. to 6:00 p.m. on May 13, 14, and 15, Fig. 7 shows the change in yield for various configurations. The hourly variance of collected water production rises as the fin spacing of the cylindrical and conical hemispherical continues to rise. The daily cumulative distillate yields for CHSWF, CyFHS (Case 1), CoFHS (Case 1), CyFHS (Case 2), CoFHS (Case 2), CyFHS (Case 3), and CoFHS (Case 3) are 4.2, 5.55, 6.2, 6, 6.65, 6.7, and 7.15 L/m2/day, respectively.
The accumulated daily yield for the three test configurations is shown in Fig. 8, with the maximum daily yield of 7.15 L/m2 achieved when the fins spacing is 4.5 cm in CoFHS (Case 3). Figure 9 shows the daily yield enhancement due to using CyFHS and CoFHS at different fins spacing, it is seen that the maximum daily yield increase of 70.24% compared to CHSWF is achieved when fins spacing is 4.5 cm in CoFHS (Case 3).
Table 4
Commulative daily yield comparisons by changing the fins spacing of cylindrical and conical hemispherical still (3, 3.75, and 4.5 cm)
Day
|
Solar Still
|
Daily yield (l)
|
Improvement rate (%)
|
13-05-2022
|
CHSWF
|
4.20
|
-
|
CyFHS (Case 1)
|
5.55
|
32.14
|
CoFHS (Case 1)
|
6.20
|
47.62
|
14-05-2022
|
CHSWF
|
4.20
|
-
|
CyFHS (Case 2)
|
6.00
|
42.86
|
CoFHS (Case 2)
|
6.65
|
58.33
|
15-05-2022
|
CHSWF
|
4.20
|
-
|
CyFHS (Case 3)
|
6.70
|
59.52
|
CoFHS (Case 3)
|
7.15
|
70.24
|
Based on the fin spacing, Fig. 10 depicts the efficiency of CyFHS and CoFHS. The average efficiency of hemispherical distillers CyFHS and CoFHS increases as the fins spacing increases because the efficiency of hemispherical distiller dependent on yield and water temperature. CHSWF, CyFHS (Case 1), CoFHS (Case 1), CyFHS (Case 2), CoFHS (Case 2), CyFHS (Case 3), and CoFHS (Case 3) have average efficiency ratings of 37.15, 48.95, 54.47, 52.95, 58.33, 58.86 and 62.72%, respectively. Figure 11 shows the enhancement in daily efficiency due to using CyFHS and CoFHS at different fins spacing, it is seen that the maximum daily efficiency enhancement of 68.08.% compared to CHSWF is achieved when fins spacing is 4.5 cm in CoFHS (Case 3).
Economic Evaluation
Table 5 shows the payback period of the CHSWF, CyFHS (Case 1), CyFHS (Case 2), CyFHS (Case 3), CoFHS (Case 1), CoFHS (Case 2), and CoFHS (Case 3) for modules with cylindrical and conical fins at various spacings, based on the overall cost of manufacturing, operating cost, and maintenance cost (3, 3.75 and 4.5 cm). The payback period for CHSWF, CyFHS (Case 1), CyFHS (Case 2), CyFHS (Case 3), CoFHS (Case 1), CoFHS (Case 2), and CoFHS (Case 3) is 36, 28, 26, 23, 25, 23 and 21 days, respectively, to recover the whole cost.
Table 5
Economic analysis of the distillers CHSWF, CyFHS (Case 1), CyFHS (Case 2), CyFHS (Case 3), CoFHS (Case 1), CoFHS (Case 2) and CoFHS (Case 3)
|
CHSWF
|
CyFHS
|
CoFHS
|
Case 1
|
Case 2
|
Case 3
|
Case 1
|
Case 2
|
Case 3
|
Capital cost (DZD)
|
9000
|
9000
|
9000
|
9000
|
9000
|
9000
|
9000
|
The price of Cement (DZD)
|
-
|
200
|
180
|
160
|
150
|
130
|
110
|
Maintenance cost (DZD)
|
50
|
50
|
50
|
50
|
50
|
50
|
50
|
Total cost (DZD)
|
9050
|
9250
|
9230
|
9210
|
9200
|
9180
|
9160
|
Productivity ((kg/m2/day)
|
4.20
|
5.55
|
6.00
|
6.70
|
6.10
|
6.65
|
7.15
|
The cost per liter of distilled water on the market (DZD)
|
60
|
60
|
60
|
60
|
60
|
60
|
60
|
The price of daily water production (DZD)
|
252
|
333
|
360
|
402
|
366
|
399
|
429
|
Payback period (Day)
|
36
|
28
|
26
|
23
|
25
|
23
|
21
|
(1$=132.78 DZD, 1€=156.03 DZD)