含氢综合能源系统是未来能源系统的重要组成，通过多类型电解槽模块协同控制有助于提升新能源消纳和制氢模块运行效率。本文建立了碱性水电解槽和质子交换膜水电解槽动态效能和启停特性模型，提出了含多类型电解槽模块的电-氢-热综合能源系统运行框架及协同优化策略，以系统运维成本、弃能成本、电解槽启停成本和制氢收益构成的综合成本最小为目标，实现各电解槽模块启停和功率优化。经修改的IEEE39节点电力-6节点热力系统验证，本文所提出的运行框架及优化策略可提升新能源消纳率，制氢系统能效提升8.13%、总成本收益增加40.83%。

Hydrogen-containing integrated energy system is an important component of the future energy system, and the synergistic control of multiple types of electrolyser modules can help to improve the consumption of new energy and the operation efficiency of hydrogen production module. In this paper, the dynamic efficiency and start-stop characteristics of alkaline water electrolyser and proton exchange membrane water electrolyser are modelled, and the operation framework and co-optimization strategy of the electric-hydrogen-thermal integrated energy system with multiple types of electrolyser modules are proposed to achieve the optimization of start-stop and power of each electrolyser module with the goal of minimizing the comprehensive cost consisting of the system operation and maintenance cost, the cost of discarded energy, the cost of starting and stopping the electrolyser, and the revenue from hydrogen production. The operation framework and optimisation strategy proposed in this paper can improve the new energy consumption rate, increase the energy efficiency of the hydrogen production system by 8.13%, and increase the total cost benefit by 40.83%, as verified by the modified IEEE 39-node power-6-node thermal system.