4.7 Article

Renewable methanol production from green hydrogen and captured CO2: A techno-economic assessment

期刊

JOURNAL OF CO2 UTILIZATION
卷 68, 期 -, 页码 -

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.jcou.2022.102345

关键词

Power -to -methanol; CO 2 hydrogenation; Renewable methanol; Techno-economic assessment

向作者/读者索取更多资源

This paper presents a pre-feasibility study on a power-to-fuel plant configuration for the production of renewable methanol. The study utilizes green hydrogen and captured carbon dioxide as raw materials. A comprehensive process model is developed to simulate the plant sections and the overall system. The economic analysis indicates that the technology is currently not competitive, but expected to become competitive in the future with the implementation of new European policies.
This paper aims to present a pre-feasibility study of a power-to-fuel plant configuration designed for the pro-duction of 500 kg/h of renewable methanol (e-methanol) from green hydrogen and captured carbon dioxide. Hydrogen is obtained by water electrolysis employing the overproduction of renewable electricity. Carbon di-oxide is assumed to be separated from the flue gas of a conventional power station by means of an amine-based CO2 absorption system. A comprehensive process model has been developed with the support of Aspen Plus tool to simulate all the plant sections and the overall system. After the process optimization, a detailed economic analysis - based on capital and operating costs derived from commercial-scale experience and assuming a 20 -year lifetime - has been performed to calculate a levelized cost of methanol (LCoM) of 960 euro/t (about 175 euro/MWh). The analysis confirms that, today, the technology is still not competitive from the economic point of view, being LCoM more than double than the current methanol price in the international market (450 euro/t). However, it indicates that the process is expected to become competitive in a mid-term future, as a consequence of the new European policies. The study also reveals that LCoM is mainly affected by the electricity price and the electrolyser capital cost, as well as the capacity factor of the plant.

作者

我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。

评论

主要评分

4.7
评分不足

次要评分

新颖性
-
重要性
-
科学严谨性
-
评价这篇论文

推荐

暂无数据
暂无数据