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Methodology for multi-objective optimization of wind turbine/battery/ electrolyzer system for decentralized clean hydrogen production using an adapted power management strategy for low wind speed conditions

机译:用于电池/电池/电池系统的多目标优化的方法,用于使用适应的电源管理策略进行低风速条件

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In this study, the utilization of renewable energy sources (RESs) like wind energy for clean hydrogen production via water electrolysis in small-scale decentralized plant is addressed. This paper proposes an approach for multiobjective optimization of wind-hydrogen production system (WHPS) while satisfying multiple technical constraints based on a dynamic power and hydrogen management strategy (PHMS). WHPS consists of wind turbines (WTs), water electrolyzer, battery bank, power converters and hydrogen tank. Multi-objective optimization consists of minimizing the total hydrogen deficit (THD), energy dump possibility (EDP), levelized cost of hydrogen (LCOH) as well as CO2 emission avoided (CO2EA) and natural gas preserved (NGP). Battery assistance for electrolyzer is enhanced through a dynamic PHMS adapted to low wind speed conditions. PHMS based multiobjective optimization algorithm is developed to find Pareto-optimal solutions. The optimization results reveal that the adequate design of PHMS plays a crucial role in minimizing THD, LCOH and EDP, while ignoring the EDP objective may reduce potentially LCOH. Under the selected base case conditions, small-scale hydrogen production via WHPS consisting of 250 kW alkaline-electrolyzer, 857.5 kW WTs, 719 kW h battery bank and 2022 kg hydrogen tank, for supplying hydrogen demand at full reliability (THD = 0%), results in LCOH of 33.70 $/kg, CO2EA of 87.75 ton/year, NGP of 28.96 ton/year and EDP of 9.96%.
机译:在这项研究中,解决了通过在小规模分散植物中通过水电解的清洁氢气产生的可再生能源(RESS)的利用。本文提出了一种基于动态功率和氢气管理策略(PHMS)的多目标优化的风氢生产系统(WHPS)的多目标优化方法。 WHP由风力涡轮机(WTS),水电解柜,电池组,电源转换器和氢气箱组成。多目标优化包括最小化总氢缺口(THD),能量倾卸可能性(EDP),氢气(LCOH)的稳定成本以及避免的二氧化碳排放(CO2EA)和保留的天然气(NGP)。通过适应低风速条件的动态PHM,可以增强电解槽的电池辅助。基于PHMS基于PLM的多目标优化算法以查找帕累托 - 最佳解决方案。优化结果表明,在最小化THD,LCOH和EDP时,PLM的足够设计在最小化,而忽略了EDP目标可能减少潜在的LCOH。在所选择的基础壳体条件下,通过WHPS由250 kW碱性电解槽,857.5 kW WTS,719 kW电池组和2022kg氢气罐组成的小规模氢气产生,用于以完全可靠性供应氢需求(THD = 0%)结果为33.70 $ 33.70 $ / kg,CO2EA为87.75吨/年,NGP为28.96吨/年,EDP为9.96%。

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