Direct conversion of simulated propene-rich bio-syngas to liquid iso-hydrocarbons via FT-oligomerization integrated catalytic process. (1st September 2018)

• Record Type: Journal Article
• Authors: Zhang, Qian; Wang, Tiejun; Weng, Yujing; Zhang, Huiyan; Vitidsant, Tharapong; Li, Yuping; Zhang, Qi; Xiao, Rui; Wang, Chenguang; Ma, Longlong
• Is Part Of: Energy conversion and management. Volume 171(2018)
• Page Start: 211
• Page End: 221
• Publication Date: 2018-09-01
• Subjects: FT-Oli -- Biomass -- Bio-syngas -- Fischer-Tropsch synthesis (FTS) -- Oligomerization -- Isomerized hydrocarbon; Direct energy conversion -- Periodicals; Energy storage -- Periodicals; Energy transfer -- Periodicals; Énergie -- Conversion directe -- Périodiques; Direct energy conversion; Periodicals; 621.3105
• DOI: 10.1016/j.enconman.2018.05.057
• Languages: English
• ISSNs: 0196-8904

Abstract

Graphical abstract: Highlights: One-step FT-Oli process for directly production gasoline-range hydrocarbons from biomass-derived syngas. Controlling of the proximity of two active components remarkably suppressed the undesired olefin hydrogenation. C5+ selectivity of 87.3% and isomerization degree reached up to 79.3% in the oil products. Abstract: The bio-syngas formed from the catalytic cracking of bio-oil include two types of useful components which are light olefin and H2, CO. The integration of FTS and olefinic polymerization seems potential way for the production of hydrocarbon bio-fuels while fully utilizing the olefin-rich bio-syngas. This work aimed to develop an integrated process for the production of liquid hydrocarbons directly from the olefin-rich bio-syngas through a one-stage process, which included the synthesis of liquid hydrocarbons via the oligomerization of light olefin over HZSM-5 along with the FT (Fischer-Tropsch) synthesis of H2, CO over FeMn catalyst. A series of integration configuration composed of Fe-based catalyst (FeMn) and acidic zeolite (HZSM-5) were investigated, it was found that the undesired hydrogenation of lower olefin on the nearby metal active site seems greatly affected the yield of C5+ . More significantly, the proximity of the two active components plays a crucial role in suppressing the undesired hydrogenation reaction and contributing to the high selectivity of liquid hydrocarbons. The optimal catalytic performance yields a high selectivity to gasoline-range hydrocarbons (87.3%) with excellent low olefin hydrogenation selectivity (7.4%). Meanwhile, the obtained gasoline-range hydrocarbon showed high degree of isomerization. The integrated transformation process potentially provides an alternative way for the production of gasoline range isomerized hydrocarbon fuels using olefin-rich bio-syngas.