Techno-Economic Optimization of the Renewable Power to Ammonia System Based on a Flexible Process

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Xiaomeng Zhang, Wei Fan, Limei Wen, Chao Huang, Heping Jin, Qian Li, Ge He, Zhongde Dai and Yiyang Dai*, 
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Abstract

With the increasing depletion of fossil energy and the environmental pollution caused by its combustion, renewable energy has entered a stage of rapid development, marking a new trend in the energy market and sustainable energy development. The renewable power to ammonia system (RePtA) offers significant potential and prospect to replace a large number of fossil fuel ammonia technologies. However, the RePtA system driven by renewable electricity will be under frequent dynamic operation due to the fluctuation of renewable energy. In this paper, combined with specific resource conditions and device scale in a certain area, this is utilized to construct a renewable energy to hydrogen network and integrate the renewable power to ammonia system. Comparing steady-state and dynamic-state to renewable power to ammonia systems, the levelized cost of energy (LCOE) is $0.64/kWh lower than the steady-state to ammonia system, and the levelized cost of ammonia (LCOA) is $0.12/kg lower. In light of the hydrogen shortage situation, purchasing electricity from the grid to ensure that the hydrogen load of the RePtA system meets the demand for ammonia production emerges as the optimal strategy in terms of production economy and stationarity, which reduces the energy cost by nearly $1.00/kWh and increases the annual profit by 20%. Finally, compared with the actual RePtA project at Inner Mongolia, Hydrogen tank capacity is more reasonable, and LCOA is reduced by 0.4$/kg; it is observed that the optimization is effective. This paper proposed that the techno-economic optimization of the renewable power to ammonia system based on a flexible process provides a theoretical basis for the implementation of large-scale green ammonia projects.

Abstract Image

基于柔性工艺的可再生能源制氨系统技术经济优化
随着化石能源的日益枯竭及其燃烧造成的环境污染,可再生能源进入了快速发展阶段,标志着能源市场和能源可持续发展的新趋势。可再生能源制氨系统(RePtA)具有替代大量化石燃料制氨技术的巨大潜力和前景。然而,由于可再生能源的波动,可再生电力驱动的RePtA系统将处于频繁的动态运行状态。本文结合某地区的具体资源条件和设备规模,利用这一点构建可再生能源制氢网络,整合可再生能源制氨系统。对比稳态和动态可再生能源制氨系统,稳态可再生能源制氨系统的平准化能源成本(LCOE)比稳态可再生能源制氨系统低0.64美元/kWh,稳态可再生能源制氨系统的平准化成本(LCOA)比稳态可再生能源制氨系统低0.12美元/kg。在氢气短缺的情况下,从生产经济性和平稳性两方面考虑,从电网购电确保RePtA系统氢气负荷满足制氨需求成为最优策略,降低能源成本近1.00美元/千瓦时,年利润提高20%。最后,与内蒙古实际RePtA项目相比,氢罐容量更合理,LCOA降低0.4美元/kg;结果表明,优化是有效的。本文提出了基于柔性工艺的可再生能源制氨系统的技术经济优化,为大规模绿色制氨项目的实施提供了理论依据。
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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
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