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임한권

Lim, Hankwon
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Techno-economic analysis: Ethane steam reforming in a membrane reactor with H-2 selectivity effect and profitability analysis

Author(s)
Jeong, SeonjuKim, SehwaLee, BoreumRyi, Shin-KunLim, Hankwon
Issued Date
2018-04
DOI
10.1016/j.ijhydene.2017.07.202
URI
https://scholarworks.unist.ac.kr/handle/201301/24473
Fulltext
https://www.sciencedirect.com/science/article/pii/S0360319917331117?via%3Dihub
Citation
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, v.43, no.15, pp.7693 - 7702
Abstract
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.
Publisher
PERGAMON-ELSEVIER SCIENCE LTD
ISSN
0360-3199
Keyword (Author)
Ethane steam reformingMembrane reactorHydrogen productionTechno-economic analysisH-2 selectivityCash flow diagram
Keyword
FERMENTATIVE HYDROGEN-PRODUCTIONOXIDATIVE DEHYDROGENATIONNATURAL-GASPD MEMBRANECOMPOSITE MEMBRANESECONOMIC-EVALUATIONSYNGAS PRODUCTIONCARBON-DIOXIDEBED MEMBRANECO2 CAPTURE

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