Ejemplo n.º 1
0
def corr_fog_mt(sher, nuss, pran, schm, rh, t_interface, t, p):
    """ fog correction for the mass transfer
        H.J.H. Brouwers, Effect of fog formation on turbulent vapor condensation with noncondensable gases,
        J. Heat Transf. 118 (1) (1996) 243–245,
        doi: 10.1115/1.2824052
        Args:
            sher:               Sherwood number
            nuss:               sensible Nusselt number
            pran:               Prandtl number
            schm:               Schmidt number
            rh:                 relative humidity
            t_interface:        temperature at the condensate interface [celsius]
            t:                  temperature in the bulk flow [celsius]
            p:                  fluid pressure [Pa]
        Returns:
            corrections factor for fog formation
    """
    p_v = rh * fpa.temperature2saturation_vapour_pressure(t)
    c_p = fpa.moist_air_heat_capacity(t, p, p_v)
    x_vbs, x_vb = fpa.__moles_fraction_mixture__(p_v, p, t)
    x_vis, x_vi = fpa.__moles_fraction_mixture__(p_v, p, t_interface)
    lmbda = fpw.enthalpy_evaporation(t)
    # c_p_alt = c_p_mixture(x_vb, t)
    # lmbda_mol = lmbda * fpa.MOLES_MASS_VAPOUR
    return (1. + (lmbda / c_p * pran / schm * (x_vb - x_vi) / (t - t_interface) * sher / nuss) ** -1) / \
           (1. + (lmbda / c_p * pran / schm * saturation_line_slope(t_interface, p)) ** -1)
Ejemplo n.º 2
0
def corr_suction_ht(sher, nuss, pran, schm, rh, t_interface, t, p):
    """ suction correction for the heat transfer
        H.J.H. Brouwers, Effect of fog formation on turbulent vapor condensation with noncondensable gases,
        J. Heat Transf. 118 (1) (1996) 243–245,
        doi: 10.1115/1.2824052
        Args:
            sher:               Sherwood number
            nuss:               sensible Nusselt number
            pran:               Prandtl number
            schm:               Schmidt number
            rh:                 relative humidity
            t_interface:        temperature at the condensate interface [celsius]
            t:                  temperature in the bulk flow [celsius]
            p:                  fluid pressure [Pa]
        Returns:
            corrections factor for suction
    """
    p_v = rh * fpa.temperature2saturation_vapour_pressure(t)
    c_p = fpa.moist_air_heat_capacity(t, p, p_v)
    c_pv = fpw.heat_capacity(t)
    x_vbs, x_vb = fpa.__moles_fraction_mixture__(p_v, p, t)
    x_vis, x_vi = fpa.__moles_fraction_mixture__(p_v, p, t_interface)
    r_t = c_pv / c_p * (sher * pran) / (schm * nuss) * np.log(
        (1 - x_vb) / (1 - x_vi))
    return -1 * r_t / (np.exp(-r_t) - 1)
Ejemplo n.º 3
0
def jakob(t_bulk, t_interface, t_in, pressure, rel_hum):
    """ Jakob number/ ratio of sensible to latent heat
        Args:
            t_bulk:             mean bulk temperature [celsius]
            t_interface:        temperature at the condensate interface [celsius]
            t_in:               inlet temperature [celsius]
            pressure:           fluid pressure at the inlet [Pa]
            rel_hum:            relative humidity at the inlet
    """
    return fpa.moist_air_heat_capacity(t_bulk, pressure, rel_hum * fpa.temperature2saturation_vapour_pressure(t_in)) * \
        (t_bulk - t_interface) / fpw.enthalpy_evaporation(t_bulk)