Combined method for producing high-quality lubricant base oil and environment-friendly aromatic hydrocarbon oil
A technology of lubricating base oil and combination method, which is applied in the direction of hydrocarbon oil treatment, petroleum industry, hydroprocessing process, etc., and can solve the problems of low yield of the target product of cracking reaction, low yield, and inability to produce environmentally friendly aromatic oil, etc.
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Embodiment 1
[0040] The raw material is Class I 250SN base oil that is dewaxed, solvent refined, and clay refined from the third-line distillate oil of Daqing, and its properties are shown in Table 1. The temperature at the top of the extraction tower is 75°C, the temperature at the bottom of the extraction tower is 35°C, and the extraction pressure is 0.1MPa. The extraction solvent is a mixed solvent of furfural and ethanol, and the ethanol content is 5% of the total solvent weight. The mass ratio is 1:1, the recovery of raffinate oil and extract oil solvent is carried out by nitrogen stripping, the residual pressure is 500mmHg, the gas injection volume is 0.5L / KG, and the temperature is 130°C. The pressure of the hydrofining / hydro-upgrading of the raffinate oil after recovering the solvent is 15.0MPa, and the volume space velocity of the hydro-finishing / hydro-upgrading (2.0h -1 / 2.0h -1 ), the volume ratio of hydrogen to oil is 1000:1, and the specific results obtained are shown in Tabl...
Embodiment 2
[0042] FF-36 (molybdenum-nickel type) and FHUDS-5 (molybdenum-cobalt type) were selected as hydrofining catalysts, and their volume ratio was 1:1. The properties of hydrorefining catalysts are shown in Table 2.
[0043] The properties of raw oil are shown in Table 1. The temperature at the top of the extraction tower is 75°C, the temperature at the bottom of the extraction tower is 35°C, and the extraction pressure is 0.1MPa. The extraction solvent is a mixed solvent of furfural and ethanol, and the ethanol content is 5% of the total solvent weight. The mass ratio is 1:1, the recovery of raffinate oil and extract oil solvent is carried out by nitrogen stripping, the residual pressure is 500mmHg, the gas injection volume is 0.5L / KG, and the temperature is 130°C. The pressure of the hydrofining / hydro-upgrading of the raffinate oil after recovering the solvent is 15.0MPa, and the volume space velocity of the hydro-finishing / hydro-upgrading (2.0h -1 / 2.0h -1 ), the volume ratio ...
Embodiment 3
[0045] FF-36 (molybdenum-nickel type) and FHUDS-5 (molybdenum-cobalt type) were selected as hydrofining catalysts, and their volume ratio was 1:1. The properties of hydrorefining catalysts are shown in Table 2.
[0046] The raw material is Class I 400SN base oil of Maoming Minus 3 and Minus 4 mixed distillate oil, which has been solvent dewaxed, solvent refined, and clay refined. The properties of the raw oil are shown in Table 1. The temperature at the top of the extraction tower is 75°C, the temperature at the bottom of the extraction tower is 35°C, and the extraction pressure is 0.1MPa. The extraction solvent is a mixed solvent of furfural and ethanol, and the ethanol content is 5% of the total solvent weight. The mass ratio is 1:1, the recovery of raffinate oil and extract oil solvent is carried out by nitrogen stripping, the residual pressure is 500mmHg, the gas injection volume is 0.5L / KG, and the temperature is 130°C. The pressure of the hydrofining / hydro-upgrading of t...
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