FIELD: chemistry.
SUBSTANCE: invention relates to Fischer-Tropsch synthesis. Fischer-Tropsch synthesis process includes feeding gaseous reactants including at least CO, H2 and CO2, into a reactor containing an iron-based catalyst, where H2 and CO are fed in a molar ratio of H2 : CO of at least 2:1, and CO2 and CO are fed in a CO2:CO ratio of at least 0.5:1; controlling the operating temperature of the reactor in the range from 260 °C to 300 °C, withdrawal of liquid product and gaseous product containing hydrocarbons, CO, H2, water and CO2, from the reactor; wherein approximation to the equilibrium of the steam reforming in the gaseous product withdrawn from the reactor according to equation 5 is less than 0.9,
where T is the operating temperature of the reactor in kelvin, and P is the partial pressure of gases CO, CO2, H2 and water vapour in the gaseous product.
EFFECT: process is characterised by low selectivity of the formation of carbon dioxide without the need for a large amount of carbon dioxide in the feed gas for Fischer-Tropsch synthesis.
15 cl, 3 dwg, 3 tbl
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Authors
Dates
2018-10-25—Published
2015-03-19—Filed