在澳大利亚背景下的氢电解槽产能投资

J. Foster, P. Graham, J. Hayward
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摘要

随着国内和全球对低温室气体排放燃料的日益关注,以及可再生发电和能源储存成本的降低,人们重新关注水电解制氢。虽然目前主要的制氢形式是天然气的蒸汽甲烷重整,但水电解是利用可再生能源制氢的主要方法。当与大规模可再生能源技术相结合时,可再生氢生产可以作为工业过程的零碳原料。在本文中,我们研究了发电、储电和氢电解槽的产能投资优化以及同一电解槽在发电和储电同时运行时的每小时最低成本。我们使用一个定制模型,能够在一年的时间范围内使用年化折扣来考虑这些。我们考虑如何设计一个到2050年成本最低的系统,通过开发未来的可变可再生资源来满足氢的摄取要求。我们研究了电解槽和可再生能源发电和存储的产能投资成本;电解槽的尺寸和使用;与绿地开发相比,已建立网络的运营概况。每个地区都规定了每年最低制氢量的要求。这一要求必须通过对PEM和由并网电能供电的碱性电解技术的新投资来满足。该模型可以根据最低利用率或“最低运行”约束,自由确定区域电解槽的总容量和一年中每小时该容量的利用率。STABLE模型(平衡能源平降成本的时空分析,改编自DIETER开源模型,适用于澳大利亚)是一个大规模的线性优化模型,最大限度地降低系统成本,同时决定每小时运行变量与传输、发电、存储和电解槽的容量投资。在澳大利亚的背景下,对下列案例的结果进行了介绍和比较:
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Hydrogen electrolyser capacity investment in the Australian context
: A growing national and global focus on low greenhouse gas emission fuels, and cost reductions in renewable electricity generation and energy storage, has given rise to renewed attention to water electrolysis to produce hydrogen. While the current dominant form of hydrogen production is steam methane reforming of natural gas, water electrolysis is the principal method of generating hydrogen from renewable energy. When coupled with large-scale renewable energy technologies, renewable hydrogen production may serve as a zero-carbon feedstock for industrial processes. In this paper, we investigate the optimisation of both capacity investment in electricity generation, electricity storage and hydrogen electrolysers as well as the hourly least-cost operation of the same electrolysers simultaneously with generation and storage operation. We use a custom model capable of considering these within a time horizon of one year using annualised discounting. We consider how to design a least-cost system out to 2050 that meets hydrogen off-take requirements through the development of prospective variable renewable resources. We study the relevant trade-offs that are shown between: capacity investments costs in electrolysers and renewable electricity generation and storage; electrolyser sizing and utilisation, and; operational profiles in established networks compared to greenfield development. In each region an annual minimum hydrogen production requirement was imposed. That requirement must be met by new investment in PEM and alkaline electrolyser technology fed by grid-connected electrical energy. The model was free to determine the aggregate regional electrolyser capacity and the utilisation of that capacity for each hour of the year subject to a minimum utilisation or “minimum run” constraint. The STABLE model (Spatial Temporal Analysis of Balancing Levelised-Cost of Energy, adapted from the DIETER open-source model to the Australian context) is a large-scale linear optimization model minimising system cost, deciding hourly operational variables simultaneously with capacity investment in transmission, generation, storage and electrolysers. Results have been presented and compared for the following cases in the Australian context:
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