I. Introduction
Gas holders are important storage and buffer devices for by-product gases in the steel industry [1], [2]. The Linz-Donawitz converter gas (LDG), produced in the steelmaking process, is first charged into the gas holders to buffer the impact of LDG rapid and intermittent generation on the pipeline system and then delivered to other production users through the pressurizer and pipeline networks for gas recycling. In the steel industry, the actual system usually contains multiple converter gas holders that run jointly, where multiple pressure sections are set up for each gas holder, and the pressure levels in every gas holder are different. The gas holder level is a key operational index of the LDG system, so it is crucial to establish an accurate mathematical model for monitoring and forecasting it [3], [4]. However, the operation process of the gas holder system presents complex transition characteristics of multiple operating conditions, posing a great challenge to their accurate modeling.