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Linear α-olefin production with Na-promoted Fe-Zn catalysts via Fischer-Tropsch synthesis.
Yang, Sunkyu; Lee, Sungwoo; Kang, Seok Chang; Han, Seung Ju; Jun, Ki-Won; Lee, Kwan-Young; Kim, Yong Tae.
Afiliação
  • Yang S; Carbon Resources Institute, Korea Research Institute of Chemical Technology Daejeon 34114 Republic of Korea ytkim@krict.re.kr.
  • Lee S; Department of Chemical and Biological Engineering, Korea University 145 Anam-ro Seoul 02841 Republic of Korea kylee@korea.ac.kr.
  • Kang SC; Carbon Resources Institute, Korea Research Institute of Chemical Technology Daejeon 34114 Republic of Korea ytkim@krict.re.kr.
  • Han SJ; Carbon Resources Institute, Korea Research Institute of Chemical Technology Daejeon 34114 Republic of Korea ytkim@krict.re.kr.
  • Jun KW; Carbon Resources Institute, Korea Research Institute of Chemical Technology Daejeon 34114 Republic of Korea ytkim@krict.re.kr.
  • Lee KY; Carbon Resources Institute, Korea Research Institute of Chemical Technology Daejeon 34114 Republic of Korea ytkim@krict.re.kr.
  • Kim YT; Advanced Materials and Chemical Engineering, University of Science & Technology Daejeon 34113 Republic of Korea.
RSC Adv ; 9(25): 14176-14187, 2019 May 07.
Article em En | MEDLINE | ID: mdl-35519344
ABSTRACT
The production of linear alpha-olefins (α-olefins) is a practical way to increase the economic potential of the Fischer-Tropsch synthesis (FTS) because of their importance as chemical intermediates. Our study aimed to optimize Na-promoted Fe1Zn1.2O x catalysts such that they selectively converted syngas to linear α-olefins via FTS at 340 °C and 2.0 MPa. The Fe1Zn1.2O x catalysts were calcined at different temperatures from 350 to 700 °C before Na anchoring. The increase in the size of the ZnFe2O4 crystals comprising the catalyst had a negative effect on the reducibility of Fe oxides and the particle size of Fe5C2 during the reaction. The Na species in the catalyst restrained the reduction of Fe1Zn1.2O x but facilitated the formation of Fe5C2. When pure Fe1Zn1.2O x was calcined at 400 °C, the corresponding catalyst (i.e., Na0.2/Fe1Zn1.2O x (400)) exhibited higher catalytic activity and stability than the other catalysts for a 50 h reaction. Compared to the other catalysts, Na0.2/Fe1Zn1.2O x (400) enabled a higher number of active Fe carbides (Fe5C2) to intimately interact with the Na species, even though the catalyst had a lower total surface basicity based on surface area. The Na0.2/Fe1Zn1.2O x (400) showed a maximum hydrocarbon yield of 49.7% with a maximum olefin selectivity of 61.3% in the C1-C32 range. Examination of the reaction product mixture revealed that the Na0.2/Fe1Zn1.2O x catalysts converted α-olefins to branched paraffins (13.9-19.5%) via a series of isomerization, skeletal isomerization, and hydrogenation reactions. The Na0.2/Fe1Zn1.2O x (400) catalyst had a relatively low consumption rate of internal olefins compared to other catalysts, resulting in the lowest selectivity for branched paraffins. The Na0.2/Fe1Zn1.2O x (400) showed a maximum α-olefin yield (26.6%) in the range C2-C32, which was 27.9-50.0% higher than that of other catalysts. The α-olefin selectivity in the C5-C12 range for the Na0.2/Fe1Zn1.2O x (400) was 37.5% relative to the total α-olefins.

Texto completo: 1 Base de dados: MEDLINE Idioma: En Ano de publicação: 2019 Tipo de documento: Article

Texto completo: 1 Base de dados: MEDLINE Idioma: En Ano de publicação: 2019 Tipo de documento: Article