Dynamic Flexibility and Screening Assessment of a 550 MW Combined-Cycle Gas-Turbine Plant With Two-Tank Molten-Salt Thermal Storage

IF 4
Energy Storage Pub Date : 2026-09-19 DOI:10.1002/est2.70517
Mwehu Banza Samson, Zheng Cao
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Abstract

The increasing penetration of variable renewable generation requires combined-cycle gas-turbine plants to follow load more frequently, while repeated cycling reduces part-load efficiency and increases thermal stress. The unresolved problem is whether a utility-scale plant retrofitted with two-tank molten-salt storage can follow a daily dispatch while respecting inventory, thermal, control, degradation, and economic constraints. This study develops a component-based MATLAB/Simulink model of a 550 MW plant and a 488.6 MWhth storage system, including the gas-turbine island, heat-recovery steam generator, steam cycle, molten-salt heater and steam generator, tanks, pumps, heat tracing, supervisory control, direct emissions, a repairable-component availability framework, a normalized thermal-cycle severity indicator, and a screening-level economic model. The design point is calibrated with deviations below 2%. Dynamic credibility is assessed through conservation checks, state-bound and limiting-case tests, and comparison with an internal transient benchmark trajectory; independent plant transient validation remains unavailable. Under a 24 h renewable-rich dispatch, net output ranges from 313.542 to 557.990 MW and daily generation is 10 296.98 MWh, 58.34 MWh above the storage-free trajectory. The storage charges 230.50 MWhth and delivers 399.20 MWhth using both initial inventory and newly stored heat; a closed tank-side balance gives a final state of charge of 9.06%. Direct carbon intensity varies from 0.302 to 0.364 tCO2/MWh. The value 1.70 × 10−4 is retained only as a normalized cycle-severity indicator, not a life fraction. With 31 USD/kWhth installed cost, an 8% discount rate, a 25-year life, and 300 equivalent cycles per year, the levelized cost of stored heat is 15.39 USD/MWhth and ranges from 11.54 to 23.08 USD/MWhth for 400 to 200 cycles. The results demonstrate that storage can widen the dispatch range and shift recovered exhaust heat to high-value periods; however, design and investment decisions require plant transient data, disclosed component maps and controller settings, material-specific degradation laws, vendor reliability data, and annual market-based optimization.

550mw双罐熔盐蓄热联合循环燃气轮机电厂动态灵活性及筛选评估
可变可再生能源发电的日益普及要求联合循环燃气轮机电厂更频繁地跟随负荷,而重复循环降低了部分负荷效率并增加了热应力。尚未解决的问题是,在考虑库存、热、控制、降解和经济限制的情况下,一个公用事业规模的工厂改造双罐熔盐储存库是否能遵循每日调度。本研究开发了一个550 MW电厂和488.6 MWhth储能系统的基于组件的MATLAB/Simulink模型,包括燃气轮机岛、热回收蒸汽发生器、蒸汽循环、熔盐加热器和蒸汽发生器、储罐、泵、伴热、监督控制、直接排放、可修复部件可用性框架、标准化热循环严重程度指标和筛选级经济模型。设计点的校准偏差小于2%。通过守恒检查、状态边界和极限情况测试以及与内部瞬态基准轨迹的比较来评估动态可信度;独立的工厂瞬态验证仍然不可用。在24小时可再生能源调度下,净输出范围为313.542至557.990兆瓦,日发电量为10 296.98兆瓦时,比无存储轨迹高58.34兆瓦时。存储费用为230.50 MWhth,并使用初始库存和新存储的热量提供399.20 MWhth;封闭的储罐侧余额使最终电荷状态为9.06%。直接碳强度变化范围为0.302 ~ 0.364 tCO2/MWh。1.70 × 10−4仅作为标准化循环严重性指标保留,而不是寿命分数。安装成本为31美元/千瓦时,折扣率为8%,寿命为25年,每年循环300次,储热的平均成本为15.39美元/兆瓦时,400至200次循环的平均成本为11.54至23.08美元/兆瓦时。结果表明,蓄热可以扩大调度范围,将回收的余热转移到高值期;然而,设计和投资决策需要工厂瞬态数据、公开的组件图和控制器设置、材料特定的降解规律、供应商可靠性数据以及年度市场优化。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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