Title
Liquid Hydrogen Production Via Hydrogen Sulfide Methane Reformation
Keywords
Cryogenic separation; Hydrogen sulfide; Hydrogen sulfide methane reformation; Liquid hydrogen production
Abstract
Hydrogen sulfide (H2S) methane (CH4) reformation (H2SMR) (2H2S + CH4 = CS2 + 4H2) is a potentially viable process for the removal of H2S from sour natural gas resources or other methane containing gases. Unlike steam methane reformation that generates carbon dioxide as a by-product, H2SMR produces carbon disulfide (CS2), a liquid under ambient temperature and pressure-a commodity chemical that is also a feedstock for the synthesis of sulfuric acid. Pinch point analyses for H2SMR were conducted to determine the reaction conditions necessary for no carbon lay down to occur. Calculations showed that to prevent solid carbon formation, low inlet CH4 to H2S ratios are needed. In this paper, we analyze H2SMR with either a cryogenic process or a membrane separation operation for production of either liquid or gaseous hydrogen. Of the three H2SMR hydrogen production flowsheets analyzed, direct liquid hydrogen generation has higher first and second law efficiencies of exceeding 80% and 50%, respectively. © 2007 Elsevier B.V. All rights reserved.
Publication Date
1-3-2008
Publication Title
Journal of Power Sources
Volume
175
Issue
1
Number of Pages
464-472
Document Type
Article
Personal Identifier
scopus
DOI Link
https://doi.org/10.1016/j.jpowsour.2007.09.079
Copyright Status
Unknown
Socpus ID
36349010840 (Scopus)
Source API URL
https://api.elsevier.com/content/abstract/scopus_id/36349010840
STARS Citation
Huang, Cunping and T-Raissi, Ali, "Liquid Hydrogen Production Via Hydrogen Sulfide Methane Reformation" (2008). Scopus Export 2000s. 10485.
https://stars.library.ucf.edu/scopus2000/10485