Humidification Dehumidification Solar Desalination System

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Humidification Dehumidification Solar Desalination System ( humidification-dehumidification-solar-desalination-system )

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Mathematics 2021, 9, 33 27 of 31 recovery. Afterwards, an extensive parametric study is conducted in which MFR of inlet air, saline water, feedwater, and the temperature of ambient air are varied. It is observed that; for all cases, the freshwater productivity rate is increased to a maximum of 15% by recovering the heat from the condensing coil. The yearly analysis of freshwater was carried out and it is observed that the freshwater productivity is increased to a maximum of ~16% in June. Furthermore, economic analysis has demonstrated that the cost of desalinated water is decreased by ~13% by recovering the heat from the condensing coil and it is 0.13 USD/litre. It is concluded that the proposed system enhances the performance of an existing HDH desalination system. However, this work is a theoretical analysis of the waste heat recovery from the condenser of the desalination system, which is finally a physical connection, in the form of piping and tubing, from the dehumidifier to the storage tank. This piping can contribute to some practical limitation in the cycle and other studies considering the ‘design for manufacturing and assembly’ are suggested before the mass-scale production. Author Contributions: Conceptualization, R.T., and N.A.S.; methodology, R.T., and N.A.S.; software, R.T.; validation, R.T. and N.A.S.; formal analysis, R.T., J.T.J., N.A.S., and S.K.; investigation, R.T., J.T.J., N.A.S., and S.K.; resources, J.T.J.; data curation, R.T.; writing—original draft preparation, R.T.; writing—review and editing, R.T., J.T.J., N.A.S., and S.K.; visualization, R.T.; supervision, N.A.S.; project administration, S.K.; funding acquisition, J.T.T. All authors have read and agreed to the published version of the manuscript. Funding: Tecnológico Nacional de México / Instituto Tecnológico Superior de Huauchinango, Av. Tecnológico No. 80, Col. 5 de Octubre, Huauchinango 73173, Puebla, México. Acknowledgments: The first author, Rasikh Tariq, is thankful for the financial support granted by CONACYT (‘Consejo Nacional de Ciencia y Tecnología’ as in Spanish); with the following details CVU no. 949314, scholarship no. 730315, to pursue a postgraduate degree in Universidad Autónoma de Yucatán, Mexico. The authors are thankful for the financial support of Instituto Tecnológico Superior de Huauchinango. The second author, Jacinto Torres Jimenez, is thankful to CONACYT for the SNI (‘Sistema Nacional de Investigadores’ as in Spanish) system. Conflicts of Interest: The authors declare no conflict of interest. The funders had no role in the design of the study; in the collection, analyses, or interpretation of data; in the writing of the manuscript, or in the decision to publish the results. Nomenclature Letters Ac Collector Area, m2 cp Specific Heat of Air, J/kg. K d Thickness of Film, m Ds Diameter of collector tubes, m E Effectiveness of dehumidifier Fs Fin efficiency FRs Collector heat removal factor F′s Collector efficiency factor g Gravitational acceleration, m/s2 h Convective Heat Transfer Coefficient, W/m2. K hnumber Enthalpy, J/kg H Enthalpy, kJ/kg I Radiation, W/m2 m Mass flow rate, kg/s M Molecular Weight of Water HDH Humidification-Dehumidification P Pressure, Pa

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