This
study was aimed to improve the SO2 desorption effect
of basic aluminum sulfate SO2-rich solution. Based on the
desorption mechanism, we first used a falling film evaporation method
to intensify heat transfer and mass transfer. Based on the falling
film desorption heat and mass transfer model, we analyzed the falling
film evaporation and desorption of basic aluminum sulfate SO2-rich solution inside the converging–diverging tube and the
smooth tube and investigated the heat and mass transfer rules under
different conditions. It was found as the quantity of SO2-rich solution increased, the heat transfer coefficient and mass
transfer coefficient of falling film evaporation both increased, but
the SO2 desorption efficiency decreased. With the rise
of the heating temperature, the three indices all increased. With
the rise of the inlet sulfur concentration, the three indices all
increased. With the rise of the aluminum concentration, the three
indices all gradually declined. With the rise of the alkalinity, the
three indices all gradually declined. Comparative analysis showed
the heat transfer coefficient and mass transfer coefficient of falling
film evaporation and SO2 desorption efficiency were 17%–29%,
33%–69%, and 6.7%–16.3% larger inside the converging–diverging
tube than the smooth tube, respectively, indicating the basic aluminum
sulfate SO2-rich solution significantly outperforms inside
the converging–diverging tube in terms of heat transfer and
mass transfer. At the heating temperature of 108 °C, liquid film
flow rate of 0.005 kg/s, sulfur concentration of 0.06 mol/L, aluminum
concentration of 20 g/L, and basicity of 20%, the SO2 desorption
efficiency inside the converging–diverging tube could reach
a high level 94.2%, compared with only 83.7% inside the smooth tube.
Moreover, correlations were obtained to predict the heat and mass
transfer coefficients.