Outlet relative humidity assumes near-saturation at the coil surface and is fixed at RHout=95%; atmospheric pressure p is fixed atatm=1013 hPa.
Left: warm, humid air (red) is cooled and dehumidified by the coil, becoming cool, dry air (blue) on the right. Bottom bar: proportions of sensible heat (red) and latent heat (blue). Condensate drips from the coil below the dew point.
Horizontal axis = dry-bulb temperature T (°C); vertical axis = humidity ratio w (g/kg DA). Red dot = inlet (In), blue dot = outlet (Out). Horizontal component = sensible heat change, vertical component = latent heat change, blue curve = saturation curve.
Saturation vapor pressure es(T) and relative humidity RH are used to determine the water-vapor partial pressure and humidity ratio w, then calculate enthalpy h on a dry-air basis.
Saturation vapor pressure (Magnus equation):
$$e_s(T) = 6.112\,\exp\!\left(\frac{17.62\,T}{243.12+T}\right)\ \text{[hPa]}$$Humidity ratio (dry-air basis):
$$w = 622\,\frac{e}{p_\text{atm}-e}\ \text{[g/kg DA]}$$Specific enthalpy of moist air:
$$h = 1.006\,T + \frac{w}{1000}\,(2501 + 1.86\,T)\ \text{[kJ/kg DA]}$$Air mass flow rate and heat loads:
$$m_a = V \cdot \rho \approx V \cdot 1.2\ \text{[kg/s]}$$ $$Q_s = m_a\,c_p\,(T_\text{in}-T_\text{out}),\quad Q_L = m_a\,\frac{w_\text{in}-w_\text{out}}{1000}\,L_v$$ $$Q_t = m_a\,(h_\text{in}-h_\text{out}) \approx Q_s + Q_L,\quad \text{SHF} = \frac{Q_s}{Q_t}$$Here, cp=1.006 kJ/(kg·K)、Lv≈2501 kJ/kg and ρ≈1.2 kg/m³ are used. The dehumidification rate is dW = ma(win-wout)/1000 × 3600 [kg/h].