Middle-East Journal of Scientific Research 12 (12): 1704-1709, 2012 ISSN 1990-9233 © IDOSI Publications, 2012 DOI: 10.5829/idosi.mejsr.2012.12.12.32 Thermo-Electrically Cooled Solar Still S. Ravindran and M.E. Dean Department of Mech. Engg., Bharath Inst. of Sci. and Tech., Bharat University, Selaiyur, Chennai-600 073, India Abstract: Solar still is a thermal device, which is capable of trap solar light energy, evaporate water and condense water vapour, to obtain distilled water. An attempt was made to augment the performance of a solar still with the use of Thermo-electric cooling arrangement. Cooling and condensing capacity was augmented by two single stage thermo-electric modules (TEM) of 80W each. This paper presents the initial data on the performance of a hybrid solar still. The yield of water from the solar still, without TEM was 700 ml per day. With TEM, the yield improved to 1200 ml per day, an improvement of 71 percent. As the initial data on the performance of a hybrid solar still gets presented it needs further experimentation. Key words: Solar Still Performance Augmentation INTRODUCTION A report by WHO /1/ has estimated that earth consists of 97.5 percent of salty seawater and 2.5 percent fresh water. Of this, fresh water 70 % is estimated to be at the polar icecaps and 30 % as soil moisture or underground aquifers. This leads to an estimate of less than 1 % of the world’s fresh water i.e. only 0.7 percent of the total amount of water on the earth is accessible for direct human use. This observation indicates the need for a new source of water. Potable/fresh water is available from rivers, lakes, ponds and wells. In the form of rain cycle, nature is carrying out the process of water desalination since ages. Potable water is required for domestic, agriculture and industries. As per the different surveys done by Lorna F., et al /2/ and MAW of KSA /3/, ocean covers 71 recent of the earth's surface-140 million square miles with a volume of 330 million cubic miles and has an average salt content of 35,000 ppm. Underground saline/brackish water contains dissolved salts of about 2,000-2,500 ppm. Brackish/saline water is strictly defined as the water with less dissolved salts than sea water but more than 500 ppm. For agricultural purposes, water containing salt content of 1000 ppm is considered as the upper limit. Modern steam power generation plant needs water with less than 10 ppm. Potable water (fresh water) suitable for human Thermoelectric Cooling consumption should not contain dissolved salts more than 500 ppm. Demand of fresh water / potable water is estimated to be in the range of 75-100 litres / person / day. Solar still converts brackish water to produces distilled water. Solar still uses a low temperature heat energy source, solar thermal energy, for its working. The solar still has a single chamber for three activities; namely (1) energy collection, (2) evaporation and (3) condensation /6/. The main aim of the project is to produce potable water for the drinking purpose by using the solar still and to improve its performance. One of the small cooling systems is Thermoelectric module. It was proposed to be used for additional condensation of the water vapour by cooling and increases the output amount of fresh water from Solar still. In this line of thinking, a hybrid solar still was fabricated and tested for its performance. Two thermoelectric coolers were used in the new design of the solar still. The solar distiller was fabricated and tested for 7 days. With the help of the modified solar still, an improvement in its performance was obtained, in the order of 58 percent. Literature Review: Solar Still: Solar stills are very simple in construction. The specialty of these distillers is that they have single chamber for heat collection, evaporation of salty water and to condense the water vapor. Brackish water or Corresponding Author: S. Ravindran, Department of Mech. Engg., Bharath Inst. of Sci. and Tech., Bharat University, Selaiyur, Chennai-600 073, India. Cell: +9840864819. 1704 Middle-East J. Sci. Res., 12 (12): 1704-1709, 2012 seawater could be used for distillation. They have a small area for heat collection, in the order of one to two square meters. Madani and Zaki /4/ developed a prototype of a simple solar still, with double slope, at King Abdul Aziz University, Kingdom of Saudi Arabia. The yield of the still was in the order of 2.8 to 3.42 l/m2d. Thermal efficiency of the system was as low as 20 to 30 percent. James /5/ analyzed the different causes of low efficiency of a solar still. Factors affecting the efficiency are (i) feeding methods, (ii) geometrical configuration, (iii) type and thickness of insulation, (iv) air circulation aspects (vi) cover material and (vii) slope of the cover. Reduction of heat conductance of glass cover due to condensing steam and presence of air were found to be the two main causes for the low yield of the solar still. Factors invariably desired for better efficiency are (i) low thermal capacity of the unit, (ii) leak proof cover and (iii) reliable basin liner insulation. Improvements in Solar Heat Collection: In order to increase the product water and thereby the efficiency of a solar still, many researchers have attempted to improve the effectiveness of the three heat transfer processes, namely, the heat collection by configuration changes, evaporation and condensation of water vapor. The hybrid stills with additional technical gadgets attached to a simple solar distiller were also tested. They also have coverage of few square meters of land. Exhaustive reviews have been presented by Tiwari et al. /6/, Raghu Raman et al. /7/ and Aref /8/. Performance of solar stills with different glazing methods like single slope; double slope and asymmetric glazing were reported. Different materials of construction like aluminum, steel, concrete, different plastics, FRP and galvanized iron were used. Different insulation materials widely used are calcium silicate, PUF, fiber glass and sawdust. Joachim Koschikowski et al., /9/ made use of a combination of solar / membrane techniques. Zaki et al /10/ tested (a set of five) solar stills to simultaneously study the effects of three different slopes of the glass sheet, heat storing rocks at the basin and mass circulation within a still with the help of a flat plate collector. Fath et al /11/ tested a still with the pyramidal configuration. Barrera /12/ developed a spherical solar still. Mohamed /13/ made an attempt to minimize the cost of a solar still with the help of appropriate technology. Improvement of Evaporation and Condensation in Simple Solar Still: Black coloured absorber floating in water was used by Riera et al /14/. Mousa et al /15/ experimented with a double exposure solar still. Cappelletti /16/ performed tests on double condensing and double evaporating system. Bassam /17/ obtained six percent improvement by cooling the glass surface with water cooling. Solar heating with multi stage or multi effect systems were tested by Ouahes et al /18/, Le et al /19/ and Tanaka et al /20/ to boost up the yield of a solar distiller. Bouchekima /21/ tested capillary film solar distiller. Ohshiro /22/ tested the effect of wicks made of polytetrafluoroethylene in a multi effect solar system. Nabil /23/ had a separate condenser in a pool of water to obtain 70 percent efficiency. Herbert /24/ developed a new approach with three sections in a solar still, namely, evaporator, condenser and absorber cum tripper. Air circulation and heat recovery were possible with the design. Badawi /25/ made use of a wiped film rotating disk evaporator in solar powered distillation plant. Hilal /26/ compared a double effect solar still with a single effect solar still. Tiwari et al /27/ conducted experiments with three different conditions of the condensing surface, which included air conditioned surroundings and by keeping ice on the condensing surface. Ravindran et al /28,29/ performed initial tests with Thermoelectrically Cooled Solar Still. Thermoelectric Cooling Module: Thermoelectric module (TEM) is solid state heat pump that dissipates heat utilizing the Peltier Effect /5/. During operation, DC current flows through the TEM to create a temperature differential across the ceramic surfaces, causing one side of the TEM to be cold and the other side hot. Nowadays commercial standard single stage TEMs are available to achieve temperature differentials in the range of 75 to 80°C. Multistage TEMs can produce chillness well below ambient temperatures, down to minus 100°C. However, with the modern growth of processing and methods of semiconductor materials, the limits may exceed this range. TEMs have several advantages over alternate cooling technologies as listed below: 1705 They have no moving parts, so the solid state construction results in high reliability. Thermoelectric are capable of heating or cooling by simply reversing the polarity, which changes the direction of heat transfer. Middle-East J. Sci. Res., 12 (12): 1704-1709, 2012 Precise temperature control, up to ±0.01°C can be maintained under steady-state conditions. In heating mode, TEMs are much more effective than conventional resistant heaters because they generate heat from the input power supplied plus additional heat generated by the heat pumping action that occurs. TEMs are available in different shapes. Typical shapes are squares, rectangles, circles and rings. EMs are available in different sizes. They are as small as 2 x 2 mm to 62 x 62 mm. TEMs are light in weight. This makes TEMs ideal for applications with tight geometric space constraints or low weight requirements when compared too much larger cooling technologies, such as conventional compressor based systems. TEMs can also be used as a power generator converting waste heat into energy as a small DC power sources in remote locations. TEMs have some disadvantages over alternate cooling technologies as listed below: The COP is lower, compared to other heat pumps. They are suitable for limited temperature differences only. In spite of the above mentioned disadvantages, thermoelectric modules are greatly used, particularly in developing countries because of their durability, low maintenance, low cost and clean environment. There is a lot of scope for developing materials specifically suited for TE cooling purpose and these can greatly improve the COP of these devices. Development of new methods to improve efficiency catering to changes in the basic design of the thermoelectric module set up like better heat transfer, miniaturization etc., can give very effective enhancement in the overall performance of thermoelectric Module. The junctions connecting the thermo elements between the hot and cold plates are interconnected using highly conducting metal (e.g. copper) strips. The sizes of conventional thermoelectric devices vary from 3 mm2 by 4 mm thick to 75 mm2 by 5 mm thick. Most of thermoelectric modules are not larger than 50 mm in length due to mechanical consideration. The height of single stage thermoelectric modules ranges from 1 to 5 mm. The modules contain 3 to 127 thermocouples. There are multistage thermoelectric devices designed to meet requirements for large temperature differentials. Multi-stage thermoelectric modules can be up to 20 mm in height, depending on the number of stages. Commonly used semiconductor material is Bismuth telluride. Modified Solar Still: Solar still was purchased from Lakshmi Solar Industries, Pune. The model number is CD 105L. TEC module was fixed on the rear of the solar still near to the centre of the horizontal line of the wall. Two TEMs of model HT8,F2,4040,TA,W6 were used in the current test. They were purchased from M/s ISA IMPEX Pvt. Ltd., Bangalore. The TEMs were fitted on the backside wall of the solar still. Sealed TEMs were preferred as the condensation is likely to occur inside the system also. A pair of small copper plates was used to fix the TEMs on the thin walls. Silica gel was used to make the joints leak proof. On the outer side, TEMs were placed, in such way that the cooler side of the TEMs will be facing the interior of the solar still while the hot side shall be pumping heat to the environment. Care was taken to maintain a good surface contact free from air packets between the copper and ceramic surfaces of the TEMs. To achieve this condition a conducting paste was used. On both the sides of the TEMs, fins / heat sinks were provided. A small fan, with plastic mountings, was used to improve the air circulation on the hot side. On the condensing side, only a heat sink was provided. Both the units were held tight with the help of bolts and nuts. A small turf was provided below the heat sinks, in order to collect the additional water condensed. In fig. 1 and 2 the different Components and the assembled view of the TEM unit are shown. Figure 6 shows the solar still with the TEMs mounted in location. The additional water turf also can be seen. Instrumenation: As the atmospheric temperature varies in accordance to the intensity of light from the sun, a Digital Lux meter was used to measure the intensity of solar radiation, fig.7. shows the Lux meter. A pair of alcohol in-glass thermometers was used to measure the atmospheric air temperature and temperature inside the solar still. Quantity of water was measured with a measuring jar of 1.2 litre capacity. Two 5A DC power sources were used to energize the TEMs. 1706 Middle-East J. Sci. Res., 12 (12): 1704-1709, 2012 Date: 16-03-2013 Sl. No. Fig. 1: Components of the TEM assembly Intensity of light Tatm Time Interval Amount of water 1200ml 1. 152 25 09:00-10:00 2. 169 26 10:00-11:00 3. 201 30 11:00-12:00 4. 232 31 12:00-01:00 5. 248 31.5 01:00-02:00 6. 241 32 02:00-03:00 7. 170 31 03:00-04:00 8. 154 28 04:00-05:00 Table 2: Amount of water collection at different sunlight intensity with installed TEC device. Date: 18-03-2013 Sl.No. Fig. 2: The TEM assembly Intensity of light Tamb Time Interval Amount of water 700ml 1. 176 24 9-10 2. 194 26 10-11 3. 255 30 11-12 4. 260 31 12-1 5. 265 31.5 1-2 6. 232 32 2-3 7. 210 32 3-04 8. 181 33 4-5 CONCLUSION Fig. 3: Fully assembled Solar Still Functioninng Exprimental Results: Table 1 and 2 show the data of water accumulated from the solar still before and after fixing the thermoelectric cooling modules. The water collection before and after fixing the TEC are 700 ml and 1200 ml respectively. This observation leads to an estimate of 58 percent improvement in performance. Table 1: Temperature and amount of water output at various intensity of sun light From the tables 1 and 2. It can be seen that the data of water accumulated from the solar still before and after fixing the thermoelectric cooling modules are different. The water collection before and after fixing the TEC are 700 ml and 1200 ml respectively. This observation leads to an estimate of improvement or augment in yield or performance of the Hybrid solar still to be 58 percent. The observation, which has been made is only a starting point in the water production in small quantities. It has to be explored further deeply. There is a need for more studies that combine several techniques, exploiting the best of each and using these practically. ACKLOWLEDGEMENT The author thanks all his colleagues Mrs. B. Sharmila, Mr. S. Brahmdeo, Mr. C. Mritunjay and Mr. M. Manish for their support during the research work. Nomenclature 1707 Middle-East J. Sci. Res., 12 (12): 1704-1709, 2012 COP ppm TEC TEM Tatm WHO MAW Coeff. of Performance parts per million Thermoelectric Cooling Thermoelectric Module atmospheric temperature World Health Organisation Ministry of Agriculture and Water 12. 13. REFERENCES 1. Claire, S., 2002. “The Last Drop”, Mazaya, Summer Issue. 2. Lorna F., et al., 1998. ‘Water Quality: Guidelines, Standards and Health, Assessment of Risk and Risk Management for Water-Related Infectious Disease’, WHO, IWA Publishing, UK. 3. Ministry of Agriculture and Water, K.S.A., 1984. “Water Atlas of Saudi Arabia”. 4. Madani, A.A. and G.M. Zaki, 1989. “Prospective of Two Small Water Producing Units”, Proc. of the 4th World IDA congress on ‘Solar Desalination and Water Reuse’, Kuwait, Nov., 4-8: 167-180. 5. James, S., 1981. Williamson, ‘Solar Distillation Process’, Proc. of the Second Workshop, Denver, Bakr H. Khoshaim (ed), James S. Williamson (ed), Midwest Research Institute. 6. Tiwari, G.N., K. Mukherjee, K.R. Ashok and Y.P. Yadav, 1986. ‘Comparison of Various Designs of Solar Stills’, Desalination, 60: 191-202. 7. Raghu Raman, Susan Mantell, Jane Davidson, Chunhui Wu and Gary Jorgensen, 2000. ‘A Review of Polymer Materials for Solar Water Heating System’, Trans. of the ASME., J of Solar Energy Engg., 122: 92-100. 8. Aref, Y., 0000. Maalej, ‘Solar Still Performance’, ENIS, Ecole Natinale D’Ingeniurs SFAX, Tunisia, pp: 207-219. 9. Joachim Koschikowski, 2002. Marcel Wieghaus, Matthias Rommel, ‘Solar Thermal Driven Desalination Plants Based on Membrane Distillation, Membranes in Drinking and Industrial Water Production’, MDIW Mülheim an der Ruhr, Germany, pp: 22-26. 10. Zaki, G.M., T. El-Dali and M. El-Shafiey, 1983. ‘Improved Performance of Solar Stills, Proc. of the First Arab International Solar Energy Conference on ‘Solar Energy and the Arab World’, Kuwait, 2-8, December 1983, Pergamon Press, pp: 331-340. 11. Fath, H.E.S., M. El-Samanoudy, K. Fahmy and 14. 15. 16. 17. 18. 19. 20. 21. 22. 23. 24. 25. 1708 A. Hassabou, 2003. ‘Thermal-Economical Analysis and Comparison Between Pyramid Configuration and Single Slope Solar Stills’, World Congress on Desalination and Water Reuse-Water for a Better Future, organized by IDA, Bahamas. Barrera, E., 1993. ‘Double Effect Spherical Solar Still’, SunWorld, 17(1): 12-14. Mohamed, M.A., 1983. ‘Solar Water Distillation Using Appropriate Technology’, Proc. of the First Arab International Solar Energy Conference on ‘Solar Energy and the Arab World’, Kuwait, 2-8, December 1983, Pergamon Press, pp: 341-345. Riera, J., J.A. Martinez-Lozano, F. Tejerina and F. Tena-Sanguesa, 1978. ‘Efficiency of a Solar Still as a Function of its Main Parameters, Production Estimation for Valencia, Spain’, Int. Symp.-Workshop on ‘Solar Energy’, Cairo, 16-22 June, T. Nejat Veziroglu (ed.), Pergamon Press Inc., NY., 3: 1570-86. Mousa, M.M., F.M. Abdelfattah and I.A. Sakr, 0000. ‘Double Exposure Solar Still’, ib id., pp: 1546-1560. Cappelletti, G.M., 2002. ‘an Experiment with a Plastic Solar, Still’ Desalination, 142: 221-227. Bassam Abu-Hijleh, K., 1996. ‘Enhanced Solar Still Performance using Water Film Cooling of the Glass Cover’, Desalination, 107: 235-244. Ouahes. R., C. Ouahes, P. Le Goff and J. Le Goff, 1987. ‘A Hardy, High-Yield Solar Distiller of Brackish Water’, Desalination, 67: 43-52. P. Le Goff, J. Le Goff and M. Razak Jeday, 0000. ‘Development of a Rugged Design of a High Efficiency Multi-Stage Solar Still’, Tanaka, H., T. Nosoko and T. Nagata, 2000. ‘A Highly Productive Basin-Type-MultipleEffect Coupled Solar Still’, Desalination, 130: 279-293. Bouchekima, B., B. Gros, R. Ouahes and M. Diboun, 1998. ‘Performance study of the Capillary Film Solar Distiller’, Desalination, 116: 185-192. Ohshiro, K., T. Nosoko and T. Nagata, 1996. ‘A Compact Solar Still Utilizing Hydrophobic Poly (tetrafluoroethylene) Nets for Separating Neighboring Wicks’, Desalination, 105: 207-217. Nabil Hussain A. Rahim, 1995. ‘Utilization of a forced Condensing Technique in a Moving Film Inclined Solar Desalination Still’, Desalination, 101: 255-262. Herbert Kunze, 2001. ‘A New Approach to Solar Desalination for Small and Medium Size use in Remote Areas’, Desalination, 139: 35-41. Badawi W. Tleimat, 1981. ‘The Use of the Wiped-Film Middle-East J. Sci. Res., 12 (12): 1704-1709, 2012 Rotating-Disk Evaporator in Solar-Powered Distillation’, ‘Solar Distillation Process’, Proc. of the Second Workshop, Denver, Bakr H. Khoshaim (ed), James S. Williamson (ed), Midwest Research Institute. 26. Hilal Al-Hinai, M.S. Al-Nassri and B.A. Jubran, 2002. ‘Parametric Investigation of a Double-Effect Solar Still in Comparison with a Single-Effect Solar Still’, Desalination, 150: 75-83. 27. Tiwari, G.N., Md. Emran. Khan and R.K. Goyal, 1998. ‘Experimental Study of Evaporation in Distillation’, Desalination, 115: 121-128. 28. Ravindran, S. et. al., 2012. “Performance of Thermoelectrically Cooled Solar Still”, B. Tech. thesis Mech. Engg. Dept., Vel Tech Technical University, (2012-13). 29. Ravindran, S., Sharmila, C. Mritunjay, S. Brahmdeo and M. Manish, 2013. ‘Performance of ThermoElectrically Cooled Hybrid Solar Still’, Proceedings of the Fortieth Nat. Conf. FMFP, NIIT, Hamirpur (HP), Dec., pp: 12-14. 1709
© Copyright 2026 Paperzz