FIELD: oil and gas industry.
SUBSTANCE: invention relates to the hydro-cracking process in which the high boiling crude hydrocarbons is converted at the temperature of 360-440°C, pressure 6-20 MPa, the raw materials mass consumption 0.5-1.5 h-1, the volume ratio of hydrogen to the raw material is 800-2000 nm3/m3 in the presence of the catalyst, containing nickel and tungsten in the form of bimetallic complex compounds of Ni (NH4)x[HyW2O5(C6H5O7)2], where: C6H5O7 - partially deprotonated form of citric acid; x = 0, 1 or 2; y = 2-x; silicon in the form of the amorphous aluminosilicate, aluminium in the form γ-Al2O3. The components in the catalyst are contained in the following concentrations, wt %: [Ni (NH4)x[HyW2O5(C6H5O7)2] - 32.6-39.6, amorphous aluminosilicate - 30.2-47.2; γ-Al2O3 the rest, which corresponds to the content of the calcined catalyst at 550C°, wt %: WO3 - 19.3-24.2, NiO - 3.0-3.8, amorphous aluminosilicate - 36.0-54.4; γ-Al2O3 - the rest.
EFFECT: high yield of middle-distillate fractions.
3 cl, 2 tbl, 5 ex
Title | Year | Author | Number |
---|---|---|---|
HYDROCARBONS CRUDE HYDROCRAKING CATALYST | 2016 |
|
RU2626396C1 |
METHOD OF PRODUCING CATALYST OF HYDROCARBON RAW MATERIAL HYDROCRAKING | 2016 |
|
RU2633965C1 |
METHOD OF HYDROCRACKING HYDROCARBON MATERIAL | 2017 |
|
RU2662232C1 |
HYDROCRACKING CATALYST OF RAW HYDROCARBON DEPOSITS | 2017 |
|
RU2662239C1 |
METHOD OF PREPARING CATALYST FOR HYDROCRACKING HYDROCARBON MATERIAL | 2017 |
|
RU2662234C1 |
METHOD OF HYDROCRACKING HYDROCARBON MATERIAL | 2015 |
|
RU2603776C1 |
CATALYST FOR HYDROCRACKING HYDROCARBON MATERIAL | 2015 |
|
RU2607905C1 |
METHOD OF PREPARING CATALYST FOR HYDROCRACKING HYDROCARBON MATERIAL | 2015 |
|
RU2607908C1 |
METHOD FOR HYDROCRACKING OF HYDROCARBON RAW MATERIALS | 2022 |
|
RU2786516C1 |
METHOD FOR PREPARING CATALYST FOR HYDROCRACKING OF HYDROCARBON FEEDS | 2022 |
|
RU2794727C1 |
Authors
Dates
2017-07-27—Published
2016-10-19—Filed