Thermodynamic limits to the productivity of passive solar distillators

Henry Alberto Salinas-Freire, Osney Pérez-Ones, Susana Rodríguez-Muñoz

Article ID: 1537
Vol 5, Issue 2, 2022

VIEWS - 291 (Abstract) 235 (PDF)

Abstract


Seawater desalination has been studied with interest due to the scarcity of fresh water for human consumption. Solar distillation is an old method; the productivity, energy consumption of the process and the cost of the desalinated water thus obtained depend on the efficiency achieved in each of the stages of these systems. The limited capacity to absorb solar radiation and transform it into useful heat for evaporation, interaction with the surrounding medium, and heat losses restrict the overall efficiency of the thermal process and productivity. Since the energy comes from solar radiation, the maximum productivity of this process will be constrained by the magnitude of the total solar radiation available in an area of the planet due to its geographic location, time of year and local climatic conditions. The processes of this energy will be thermodynamically limited by the heat transfer coefficients achieved in the equipment, the maximum value that the evaporation heat can reach, as long as the losses to the environment by convection and radiation are minimal. Comparative analyses of several proposed models, reported data of distillers, reported data of solar radiation that reach average values of up to 7.2–7.4 kwh/m2 in some regions of the planet are presented and estimates are made for productivity of these equipments that they reach between 6.7 and 6.9 kg/m2 day with a theoretical maximum efficiency of about 0.16 of the total solar radiation.


Keywords


Desalination; Passive Solar Distiller; Solar Distiller Productivity; Solar Distiller Efficiency

Full Text:

PDF


References


1. Dwivedi VK, Tiwari GN. Experimental validation of thermal model of a double slope active solar still under natural circulation mode. Desalination 2010; 250(1): 49–55.

2. Hernández H, Rubalcaba E, Hermosillo JJ. Improvement of a MEH desalination unitby means of heat recovery. Energy Procedia 2014; 57: 2781–2786.

3. Moya EZ. Desalinización del agua del mar mediante energías renovables (Spanish) [Desalination of sea water using renewable energies]. Instituto de Estudios Almerienses: Actas del I y II seminario del agua; 1997. p. 199–226.

4. Tiwari GN, Singh HN, Tripathi R. Present status of solar distillation. Solar Energy 2003; 75(5): 367–373.

5. Moore BA, Martinson E, Raviv D. Waste to water: A low energy water distillation method. Desalination 2008; 220(1-3): 502–505.

6. Youssef PG, Al-Dadah RK, Mahmoud SM. Comparative analysis of desalination technologies. Energy Procedia 2014; 61: 2604–2607.

7. Al-Weshahi MA, Tian G, Anderson A. Performance enhancement of MSF desalination by recovering stage heat from distillate water using internal heat exchanger. Energy Procedia 2014; 61: 381–384.

8. Darwish M. Qatar water problem and solar desalination. Desalination and Water Treatment 2014; 52(7-9): 1250–1262.

9. Khayet M. Solar desalination by membrane distillation: Dispersion in energy consumption analysis and water production costs (a review). Desalination 2013; 308: 89–101.

10. Ma Q, Yi C, Lu H, et al. A conceptual demonstration and theoretical design of a novel “super-gravity” vacuum flash process for seawater desalination. Desalination 2015; 371: 67–77.

11. El-Sebaii AA, El-Bialy E. Advanced designs of solar desalination systems: A review. Renewable and Sustainable Energy Reviews 2015; 49: 1198–1212.

12. Asiedu-Boateng P, Nyarko BJB, Yamoah S, et al. Comparison of the cost of co-production of power and desalinated water from different power cycles. Energy and Power Engineering 2013; 5(1): 26–35.

13. Hamed OA, Kosaka H, Bamardouf KH, et al. Concentrating solar power for seawater thermal desalination. Desalination 2016; 396: 70–78.

14. Gabriel KJ, Linke P, El-Halwagi MM. Optimization of multi-effect distillation process using a linear enthalpy model. Desalination 2015; 365: 261–276.

15. Compain P. Solar energy for water desalination. Procedia Engineering 2012; 46: 220–227.

16. Abdelmoez W, Mahmoud MS, et al. Water desalination using humidification/dehumidification (HDH) technique powered by solar energy: A detailed review. Desalination and Water Treatment 2014; 52(25-27): 4622–4640.

17. Abdallah SB, Frikha N, Gabsi S. Study of the performances of different configurations of seawater desalination with a solar membrane distillation. Desalination and Water Treatment 2014; 52(13-15): 2362–2371.

18. Cooper PI. The maximum efficiency of single-effect solar stills. Solar Energy 1973; 15(3): 205–217.

19. Kumar S, Tiwari GN. Estimation of convective mass transfer in solar distillation systems. Solar Energy 1996; 57(6): 459–464.

20. Goosen MF, Sablani SS, Shayya WH, et al. Thermodynamic and economic considerations in solar desalination. Desalination 2000; 129(1): 63–89.

21. Sharma VB, Mullick SC. Estimation of heat-transfer coefficients, the upward heat flow, and evaporation in a solar still. Journal of Solar Energy Engineering 1991; 113(1): 36–41.

22. Aboul-Enein S, El-Sebaii AA, El-Bialy E. Investigation of a single-basin solar still with deep basins. Renewable Energy 1998; 14(1-4): 299–305.

23. Yeh HM, Ma NT. Energy balances for upward-type, double-effect solar stills. Energy. 1990; 15(12): 1161–1169.

24. Al-Hayeka I, Badran OO. The effect of using different designs of solar stills on water distillation. Desalination 2004; 169(2): 121–127.

25. ESMAP. Global Horizontal Irradiance Poster Map. Solargis; 2017. Available from: www.worldbankgroup.com.

26. Sampathkumar K, Arjunan T, Pitchandi P, et al. Active solar distillation—A detailed review. Renewable and Sustainable Energy Reviews 2010; 14(6): 1503–1526.

27. Dunkle RV. Solar water distillation: The roof type still and a multiple effect diffusion still. Proc. International Heat Transfer Conference; 1961 Jan 8-12; University of Colorado, USA. 1961. p. 895.

28. Smith JM, Van Ness HC, Abbott MM. Introduction to thermodynamics in Chemical Engineering. 7th ed. Mexico: Interamericana M-H; 2007.

29. Cengel Y. Heat and mass transfer (a practical approach). 3rd ed. Mexico: McGraw Hill; 2007.

30. Setoodeh N, Rahimi R, Ameri A. Modeling and determination of heat transfer coefficient in a basin solar still using CFD. Desalination 2011; 268(1-3): 103–110.

31. Shukla SK, Sorayan VPS. Thermal modeling of solar stills: An experimental validation. Renewable Energy 2005; 30(5): 683–699.

32. Tiwari GN, Shukla SK, Singh IP. Computer modeling of passive/active solar stills by using inner glass temperature. Desalination 2003; 154(2): 171–185.

33. Mowla D, Karimi G. Mathematical modelling of solar stills in Iran. Solar Energy 1995; 55(5): 389–393.

34. Dev R, Tiwari GN. Characteristic Equation of a passive solar still. Desalination 2009; 245(13): 246–265.

35. Perry RH. Green DW. Perry’s Chemical Engineers Handbook. 8th ed. In: Hill M (editor). New York: McGraw Hill; 2008. p. 2735.




DOI: https://doi.org/10.24294/tse.v5i2.1537

Refbacks

  • There are currently no refbacks.


Copyright (c) 2022 Henry Alberto Salinas-Freire, Osney Pérez-Ones, Susana Rodríguez-Muñoz

Creative Commons License
This work is licensed under a Creative Commons Attribution-NonCommercial 4.0 International License.

This site is licensed under a Creative Commons Attribution 4.0 International License.