I. Introduction
SO2 pollution has drawn increasing concern due to its detrimental effects on ambient atmosphere and human health [1]. One of major contributors to SO2 emissions are various types of fossil fuels-based power plants, among which the coal-fired power plant is found most commonly in practice. Due to this fact, the ultra-low SO2 emission concentration of 35mg/m3 is required by the Chinese government, which is the most stringent SO2 emission standard in history [2]. To achieve this target, FGD technologies are widely employed in SO2 emitting processes, where alkaline absorbents such as sodium hydroxide (NaOH), calcium oxide (CaO) and limestone (CaCO3), etc. are used to react with sulfur dioxide exists in the released flue gas. Among all FGD technologies, the limestone-based wet FGD plays a dominant role due to its cost-effectiveness and high reliability [3]. As the operating status of FGD system has a substantial effect on the desulfurization performance, it is essential to well understand the dynamic behavior of the FGD process. Consequently, a lot of research interests have been in the FGD process modeling; however FGD is a nonlinear multivariable process with high time delay, rendering the modeling task a real challenge. The modeling approaches can be separated into two categories: mechanism-based approaches and data driven approaches.