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Direct synthesis of isopaxaffin from synthesis gas under supercritical conditions
Yoneyama, Yoshiharu1; Sun, Xiaoyu2; Zhao, Tiansheng3; Wang, Tiejun4; Iwai, Toshiaki1; Ozaki, Koichi1; Tsubaki, Noritatsu1,5
2010-01-15
Source PublicationCATALYSIS TODAY
Volume149Issue:1-2Pages:105-110
AbstractTo produce isoparaffins from synthesis gas directly, modified Fischer-Tropsch (FT)synthesis was carried out under supercritical conditions using n-butane as a medium. One-step FT synthesis using a hybrid catalyst consisting Of Co/SiO(2), HZSM-5 and Pd/SiO(2) was carried Out Introduction of supercritical-phase n-butane increased light isoparaffins significantly and suppressed the formation of the by-product, methane. Under supercritical-phase butane. hydrogenolysis and isomerization reactions were promoted. Due to the fact that the optimum temperatures for FT and HZSM-5 catalysts are different. 513 K and over 573 K, respectively. two-step FT synthesis was also carried Out to optimize the reaction temperatures. The first-step reaction used Co/SiO(2) catalyst containing small amount of HZSM-5 for FT synthesis at 513 K, and the second-step reaction used a hybrid catalyst containing Pd/SiO(2) and zeolite for hydrogenolysis and isomerization of hydrocarbons at 573 K Introduction of supercritical n-butane increased the isoparaffin selectivity, and decreased the methane selectivity significantly. The production of heavy hydrocarbons C(9)(+) was inhibited in both gas and supercritical phase. The isoparaffin selectivity in the gas phase decreased with time-on-stream, but very stable for the supercritical-phase reaction Because water and heavy hydrocarbons were removed from active sites on zeolite and the zeolite acidity was promoted in the supercritical medium. the selectivity of isoparaffin was considered stable Among zeolites added to the hybrid catalyst in the second-step reactor. HZSM-5 and H-beta zeolite were suitable for producing light isoparaffins. These results indicated that two-step FT synthesis under supercritical n-butane was superior for producing light isoparaffins from synthesis gas directly. (C) 2009 Elsevier B.V. All rights reserved
SubtypeArticle
KeywordFischer-tropsch Synthesis Hzsm-5 Supercritical Conditions
WOS HeadingsScience & Technology ; Physical Sciences ; Technology
DOI10.1016/j.cattod.2009.03.021
WOS Subject ExtendedChemistry ; Engineering
WOS KeywordFISCHER-TROPSCH SYNTHESIS ; HYBRID CATALYST ; ISOPARAFFIN
Indexed BySCI ; ISTP
Language英语
WOS SubjectChemistry, Applied ; Chemistry, Physical ; Engineering, Chemical
WOS IDWOS:000274145600016
Citation statistics
Cited Times:8[WOS]   [WOS Record]     [Related Records in WOS]
Document Type期刊论文
Identifierhttp://ir.giec.ac.cn/handle/344007/10323
Collection中国科学院广州能源研究所
Affiliation1.Toyama Univ, Grad Sch Engn, Dept Environm Appl Chem, Toyama 9308555, Japan
2.China Univ Petr, Dongying 257061, Shandong, Peoples R China
3.Ningxia Univ, Ningxia 750021, Peoples R China
4.CAS, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China
5.CREST, JST, Chiyoda Ku, Tokyo 1020075, Japan
Recommended Citation
GB/T 7714
Yoneyama, Yoshiharu,Sun, Xiaoyu,Zhao, Tiansheng,et al. Direct synthesis of isopaxaffin from synthesis gas under supercritical conditions[J]. CATALYSIS TODAY,2010,149(1-2):105-110.
APA Yoneyama, Yoshiharu.,Sun, Xiaoyu.,Zhao, Tiansheng.,Wang, Tiejun.,Iwai, Toshiaki.,...&Tsubaki, Noritatsu.(2010).Direct synthesis of isopaxaffin from synthesis gas under supercritical conditions.CATALYSIS TODAY,149(1-2),105-110.
MLA Yoneyama, Yoshiharu,et al."Direct synthesis of isopaxaffin from synthesis gas under supercritical conditions".CATALYSIS TODAY 149.1-2(2010):105-110.
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