Efficient and Stable Production of Long-Chain Hydrocarbons over Hydrophobic Carbon-Encapsulated TiO2-Supported Ru Catalyst in Fischer-Tropsch Synthesis

被引:7
作者
Liu, Yunhao [1 ,2 ]
Li, Xincheng [1 ,2 ]
Cheng, Qingpeng [1 ,3 ]
Tian, Ye [1 ,2 ]
Zhang, Yingtian [1 ,2 ]
Ding, Tong [1 ,2 ]
Song, Song [1 ,2 ]
Song, Kepeng [4 ]
Li, Xingang [1 ,2 ]
机构
[1] Tianjin Univ, Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Tianjin Key Lab Appl Catalysis Sci & Engn, Sch Chem Engn & Technol,State Key Lab Chem Engn,Ha, Tianjin 300350, Peoples R China
[2] Zhejiang Inst Tianjin Univ Shaoxing, Shaoxing 312300, Zhejiang, Peoples R China
[3] King Abdullah Univ Sci & Technol KAUST, Adv Membranes & Porous Mat AMPM Ctr, Phys Sci & Engn Div, Thuwal 239556900, Saudi Arabia
[4] Shandong Univ, Sch Chem & Chem Engn, Jinan 250100, Peoples R China
基金
中国国家自然科学基金;
关键词
Fischer-Tropsch synthesis; ruthenium catalyst; sintering; hydrophobicity; metal-supportinteraction; SUPPORTED RUTHENIUM NANOPARTICLES; PARTICLE-SIZE DISTRIBUTIONS; SELECTIVE CONVERSION; RU/MNCO3; CATALYSTS; CO2; HYDROGENATION; COBALT CATALYSTS; SYNTHESIS GAS; ZEOLITE; SYNGAS; DEACTIVATION;
D O I
10.1021/acscatal.4c02979
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The sintering of metal catalysts caused by Ostwald ripening (OR) and particle migration and coalescence (PMC) is one of the major challenges in heterogeneous catalysis. Here, we develop an efficient Ru catalyst supported on hydrophobic carbon-encapsulated TiO2 for Fischer-Tropsch synthesis (FTS). Combining comprehensive characterizations, we discover that hydrophobic carbon layers predominantly obstruct OR, and appropriate metal-support interactions avoid PMC. The dual effects collectively prevent the aggregation and sintering of diminutive Ru nanoparticles (NPs) during the FTS process and induce robust catalytic performance. Moreover, this unique structure exposes more Ru sites to promote CO hydrogenation and diminishes Ru-TiO2 interfaces to adsorb more *CO and fewer *H species, which facilitates the production of longer-chain hydrocarbons. Consequently, at 220 degrees C, our catalyst exhibits a superior turnover frequency (TOF) of 0.189 s(-1) and a Ru time yield of 2.67 mol(CO) g(Ru)(-1) h(-1), surpassing those of the reported Ru-based catalysts. Simultaneously, the catalyst shows a C5+ selectivity of 85.3% and is particularly effective in producing C15+ (soft paraffin), with a selectivity of 57.3%. Our catalyst design strategy holds promise for efficient catalytic processes in various industrial applications.
引用
收藏
页码:10365 / 10375
页数:11
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