Maximov Anton Lvovich, Kulikova Mayya Valerevna, Dementyeva Oksana Sergeevna, Ponomareva Anna Konstantinovna
A. V. Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences (RAS), Moscow, Russia.
Faculty of Fundamental Physics and Chemical Engineering, Lomonosov Moscow State University, Moscow, Russia.
Front Chem. 2020 Nov 16;8:567848. doi: 10.3389/fchem.2020.567848. eCollection 2020.
Nanosized catalyst dispersions have significant potential for improving hydrocarbon production from carbon monoxide and hydrogen via Fischer-Tropsch synthesis, an essential alternative to the use of petroleum as a raw material. New dispersed cobalt catalysts and dispersed-phase cobalt-based catalysts with Pd, AlO, or ZrO additives for the Fischer-Tropsch synthesis were synthesized in the present work. A dispersed cobalt phase was prepared in a heavy paraffin medium using and approaches through thermal decomposition of a nitrate precursor at various temperatures. Analyses showed that an increase in the temperature for catalytic suspension formation from 215 to 260°C enlarged the particles in the dispersed phase from 190 to 264 nm, which was probably due to increased agglomeration at elevated temperatures. The rheological properties of the obtained catalytic suspensions can be described by the Bingham equation. Furthermore, the concentration of the dispersed phase had a direct impact on the structure of the entire catalytic system. Ultrafine suspensions of palladium-promoted catalytic systems were tested for the Fischer-Tropsch synthesis. The overall yield of C hydrocarbons was as high as 50 g/m, and the productivity of the Pd-promoted catalytic systems reached 270-290 g/(kg · h).
纳米催化剂分散体在通过费托合成提高由一氧化碳和氢气生产碳氢化合物方面具有巨大潜力,费托合成是替代使用石油作为原料的重要方法。在本工作中,合成了用于费托合成的新型分散钴催化剂以及含有钯、氧化铝或氧化锆添加剂的分散相钴基催化剂。通过在重质石蜡介质中使用[具体方法1]和[具体方法2],在不同温度下对硝酸盐前驱体进行热分解来制备分散钴相。分析表明,催化悬浮液形成温度从215℃升高到260℃时,分散相中的颗粒从190nm增大到264nm,这可能是由于高温下团聚增加所致。所得催化悬浮液的流变特性可用宾汉方程描述。此外,分散相的浓度对整个催化体系的结构有直接影响。对钯促进的催化体系的超细悬浮液进行了费托合成测试。碳氢化合物的总产率高达50g/m,钯促进的催化体系的生产率达到270 - 290g/(kg·h)。