FIELD: technological processes.
SUBSTANCE: invention relates to a catalyst for hydrogenating olefins during the production of synthetic oil. Catalyst comprising 41–60 % by weight of nickel from the mass of the calcined catalyst and a carrier, which is a mesoporous alumina with an average particle size of 3–7 nm, a total pore volume of at least 0.85 cm3/g, the proportion of mesopores is not less than 90 % and the specific surface area is not less than 280 m2/g. Invention also relates to methods (options) for the preparation of the catalyst described above.
EFFECT: technical result is to increase the degree of hydrogenation of olefins contained in the synthetic hydrocarbons of the Fischer-Tropsch process, more than 96 %.
3 cl, 1 tbl, 12 ex
Title | Year | Author | Number |
---|---|---|---|
CATALYST FOR RECEIVING SYNTHETIC LIGHT OLEFINS C-C FROM SYNTHESIS GAS AND METHOD OF ITS OBTAINING | 2018 |
|
RU2679801C1 |
CATALYST FOR PRODUCING SYNTHETIC HYDROCARBONS WITH HIGH CONTENT OF ISOALKANES AND METHOD OF ITS PRODUCTION | 2017 |
|
RU2672357C1 |
CATALYST FOR FISCHER-TROPSCH PROCESS IN COMPACT VERSION AND PRODUCTION METHOD THEREOF (VERSIONS) | 2015 |
|
RU2610526C2 |
METHOD OF OBTAINING SYNTHETIC OIL | 2017 |
|
RU2656601C1 |
CATALYST FOR SYNTHESIS OF HYDROCARBONS FROM CO AND H AND METHOD OF PRODUCTION THEREOF | 2022 |
|
RU2821943C2 |
MESOPOROUS MATERIALS WITH ACTIVE METALS | 2003 |
|
RU2334554C2 |
METHOD FOR OBTAINING SYNTHETIC LIQUID FUELS FROM HYDROCARBON GASES AS PER FISCHER-TROPSCH METHOD, AND CATALYSTS USED FOR ITS IMPLEMENTATION | 2010 |
|
RU2444557C1 |
MESOPOROUS BIMETALLIC FISCHER-TROPSCH SYNTHESIS CATALYST | 2022 |
|
RU2799070C1 |
CATALYST FOR DIRECT PRODUCTION OF ISOPARAFFIN-RICH SYNTHETIC OIL AND METHOD FOR PRODUCTION THEREOF | 2012 |
|
RU2524217C2 |
METHANE AROMATISATION CATALYST, METHOD FOR PRODUCTION THEREOF AND METHOD OF CONVERTING METHANE TO PRODUCE AROMATIC HYDROCARBONS | 2015 |
|
RU2585289C1 |
Authors
Dates
2018-11-13—Published
2017-08-08—Filed