Merge 25002eeb9c
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5e2c5ca5ae
@ -169,7 +169,10 @@ public:
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const Evaluation& pressure,
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const Evaluation& pressure,
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bool extrapolate = false)
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bool extrapolate = false)
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{
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{
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return tabulatedEnthalpy.eval(temperature, pressure, extrapolate);
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// TEST 2nd degree polynomial fitted with Coolprop data in temperature
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// range (273.15, 403.15) with reference state T=288.15 K (=15 C) and p = 101325 Pa
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return (temperature - 273.15 - 15)*(8.42323594e+02 + 4.54513769e-01*(temperature - 273.15 - 15)) - 0.005 * (pressure - 1.01325e5);
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// return tabulatedEnthalpy.eval(temperature, pressure, extrapolate);
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}
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}
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/*!
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/*!
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@ -635,10 +635,10 @@ private:
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/* heat of dissolution for CO2 according to Fig. 6 in Duan and Sun 2003. (kJ/kg)
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/* heat of dissolution for CO2 according to Fig. 6 in Duan and Sun 2003. (kJ/kg)
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In the relevant temperature ranges CO2 dissolution is
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In the relevant temperature ranges CO2 dissolution is
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exothermal */
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exothermal */
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delta_hCO2 = (-57.4375 + T * 0.1325) * 1000/44;
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// delta_hCO2 = (-57.4375 + T * 0.1325) * 1000/44;
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/* enthalpy contribution of CO2 (kJ/kg) */
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/* enthalpy contribution of CO2 (kJ/kg) */
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hg = CO2::gasEnthalpy(T, p, extrapolate)/1E3 + delta_hCO2;
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hg = CO2::gasEnthalpy(T, p, extrapolate)/1E3; //+ delta_hCO2;
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/* Enthalpy of brine with dissolved CO2 */
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/* Enthalpy of brine with dissolved CO2 */
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return (h_ls1 - X_CO2_w*hw + hg*X_CO2_w)*1E3; /*J/kg*/
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return (h_ls1 - X_CO2_w*hw + hg*X_CO2_w)*1E3; /*J/kg*/
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