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Feasibility study of a combined Ocean Thermal Energy Conversion method in South Korea

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Feasibility study of a combined Ocean Thermal Energy Conversion method in South Korea ( feasibility-study-combined-ocean-thermal-energy-conversion-m )

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H. Jung, J. Hwang / Energy 75 (2014) 443e452 445 Fig. 1. Simplified heat balance diagram of the PRC. should be condensed at a temperature slightly higher than that of the deep sea water. As alternative working fluids, we selected R32, R125, R134A, R143A and R410A, all of which satisfy the conditions noted above. Table 1 shows the saturation pressures of the working fluids and other characteristics of the PRC considered here at different temperatures of 10 C, 15 C, 25 C, and 30 C. The oper- ating pressure of the C-OTEC system will be determined within the saturated vapor interval depending on the refrigerant. Table 1 Refrigerant thermodynamic properties. Temp. 30.0 C 25.0C P 1690 1378 665.8 1262 15.0 C P 1281 1050 488.7 964.3 1254 10.0 C h_fg P Fig. 2. C-OTEC configuration. Property P R32 1928 R125 1568 R134A 770.6 R143A 1435 R410A 1883 v h_fg v h_fg 270.9 110.2 177.8 159.3 239.7 v v h_fg 0.0009807 298.9 0.01732 124.7 0.000793 190.7 0.02693 177.4 0.0008861 6.8 0.001064 260.4 0.009486 104.6 0.02662 173.1 0.001101 152.5 0.01307 248.3 0.001041 0.01101 0.0008287 0.01734 0.01517 0.0009991 0.0008027 0.0008042 0.001031 0.02048 290.1 1107 120.2 909.2 186.6 414.9 171.7 836.7 223.4 1085 1652 In this table, P is the saturation pressure in kPa at the given temperature, v is the specific volume in m3/kg, and h_fg is the gas enthalpy minus the fluid enthalpy in kJ/kg.

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Feasibility study of a combined Ocean Thermal Energy Conversion method in South Korea

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