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Optimal Design and Decision for Combined Steam Reforming Process with Dry Methane Reforming to Reuse CO2 as a Raw Material

Authors
Lim, YoungsubLee, Chul-JinJeong, Yeong SuSong, In HyoupLee, Chang JunHan, Chonghun
Issue Date
Apr-2012
Publisher
AMER CHEMICAL SOC
Citation
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, v.51, no.13, pp 4982 - 4989
Pages
8
Journal Title
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
Volume
51
Number
13
Start Page
4982
End Page
4989
URI
https://scholarworks.bwise.kr/cau/handle/2019.sw.cau/48815
DOI
10.1021/ie200870m
ISSN
0888-5885
1520-5045
Abstract
Carbon dioxide (CO2) conversion technology has been estimated as a potentially practical solution for global warming problems although it still has some weaknesses such as cost and energy consumption. In this study, a combined steam reforming process with dry methane reforming process for the CO2 treatment was investigated. Because the dry methane reforming process could generate synthesis gas from carbon dioxide, it could decrease the CO2 emissions from the existing steam reforming process. Models for the steam reforming process and the combined process were developed and extended mitigation cost was suggested to evaluate CO2 reduction of the overall process. The combined process could reduce net CO2 emission by 67% compared with the reference steam reforming process, and the extended mitigation cost of the combined process ranged from 21 to 26.5 (US$/CO2 ton) according to the change of the cost for CO2 transportation.
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