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Catalytic technologies for CO hydrogenation for the production of light hydrocarbons and middle distillatesoa mark
  • Chae, Ho Jin ;
  • Kim, Jin Ho ;
  • Lee, Soo Chool ;
  • Kim, Hyo Sik ;
  • Jo, Seong Bin ;
  • Ryu, Jae Hong ;
  • Kim, Tae Young ;
  • Lee, Chul Ho ;
  • Kim, Se Jeong ;
  • Kang, Suk Hwan ;
  • Kim, Jae Chang ;
  • Park, Myung June
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Publication Year
2020-01-01
Publisher
MDPI
Citation
Catalysts, Vol.10
Keyword
Acidic site controlActive metal sizeCatalyst designFischerHydrocarbonsSyngasTropsch
All Science Classification Codes (ASJC)
CatalysisPhysical and Theoretical Chemistry
Abstract
In South Korea, where there are no resources such as natural gas or crude oil, research on alternative fuels has been actively conducted since the 1990s. The research on synthetic oil is subdivided into Coal to Liquid (CTL), Gas to Liquid (GTL), Biomass to Liquid (BTL), etc., and was developed with the focus on catalysts, their preparation, reactor types, and operation technologies according to the product to be obtained. In Fischer–Tropsch synthesis for synthetic oil from syngas, stability, CO conversion rate, and product selectivity of catalysts depends on the design of their components, such as their active material, promoter, and support. Most of the developed catalysts were Fe-and Co-based catalysts and were developed in spherical and cylindrical shapes according to the reactor type. Recently, hybrid catalysts in combination with cracking catalysts were developed to control the distribution of the product. In this review, we survey recent studies related to the design of catalysts for production of light hydrocarbons and middle distillates, including hybrid catalysts, encapsulated core–shell catalysts, catalysts with active materials with well-organized sizes and shapes, and catalysts with shape-and size-controlled supports. Finally, we introduce recent research and development (R&D) trends in the production of light hydrocarbons and middle distillates and in the catalytic processes being applied to the development of catalysts in Korea.
ISSN
2073-4344
Language
eng
URI
https://dspace.ajou.ac.kr/dev/handle/2018.oak/31114
DOI
https://doi.org/10.3390/catal10010099
Fulltext

Type
Review
Funding
Funding: This work was supported by the Korea Institute of Energy Technology Evaluation and Planning (KETEP) grant funded by the Ministry of Trade, Industry & Energy (MOTIE) of the Republic of Korea (No.20173010050110). This research was supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education (NRF-2019R1A6A3A01096215).
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Park, Myung-June Image
Park, Myung-June박명준
Department of Chemical Engineering
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