4.7 Article Proceedings Paper

Techno-economic analysis: Ethane steam reforming in a membrane reactor with H2 selectivity effect and profitability analysis

期刊

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
卷 43, 期 15, 页码 7693-7702

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2017.07.202

关键词

Ethane steam reforming; Membrane reactor; Hydrogen production; Techno-economic analysis; H-2 selectivity; Cash flow diagram

资金

  1. Korea Institute of Energy Technology Evaluation and Planning (KETEP) from the Ministry of Trade, Industry & Energy, Republic of Korea [20143030030770]
  2. Korea Evaluation Institute of Industrial Technology (KEIT) [20143030030770] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

向作者/读者索取更多资源

With the increased production of shale gas through a new drilling technology of hydraulic fracturing, much attention has been directed to various utilization methods for ethane accounting for about 7% of shale gas. As an efficient utilization method for ethane, ethane steam reforming in a membrane reactor is proposed in this paper to provide improved reactant conversions and product yields thus leading to a reduced operating temperature. To assess techno-economic feasibility of ethane steam reforming in a membrane reactor, parametric studies focusing on a H-2 selectivity and economic analysis predicting profitability from cash flow diagrams based on a purified hydrogen in Korea were performed simultaneously providing very useful design and economic guidelines to implement a membrane reactor for ethane steam reforming. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.

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