The mass transfer performance of SO 2 absorption in an aqueous solution of a newly proposed organic amine absorbent, N,N′-bis(2-hydroxypropyl)piperazine (HPP), was studied by the dynamic absorption method in a θ-ring packed column. The absorption performance was interpreted in terms of the overall mass transfer coefficient, K G a. The experimental results showed that the K G a value increased with an increase in the liquid flow rate, concentration, and initial pH of HPP absorbent. However, it decreased with an increase in temperature, SO 2 partial pressure, and gas flow rate. An empirical correlation for the overall mass transfer coefficient is subsequently developed as a function of the process parameters. The obtained K G a from empirical correlation is found to be in relatively good agreement with the experimental results with a mean relative deviation of 6.6%, which could be used for engineering design.