Hydrogen donating thermal cracking method
A technology of thermal cracking and hydrogen supply, which is applied in hydrocarbon oil cracking, petroleum industry, liquid carbon-containing fuel, etc., to achieve the effects of cost saving, product stability improvement and low viscosity
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Embodiment 1
[0032] Hydrocarbon raw material A (a kind of atmospheric residue, wherein saturated content 16.56wt%, aromatic content 41.74wt%, colloid 30.16wt%, asphaltenes 11.54wt%, Ni+V metal content is 530 μ g / g, sulfur, Nitrogen content is 4.31wt%, 0.71wt% respectively) add hydrogen donor HDA to carry out small test in the laboratory, the reaction temperature is 425 ℃, the reaction is 0.4MPa(G), and the reaction time is 10min. As a result, the spot test grades of the obtained hydrogen-donating thermal cracking oil and modified oil were both grade 2 (determined according to the spot test method for cleanliness and compatibility of residual fuel oil in ASTM D4740), and the hydrogen-donating thermal cracking produced oil and modified oil The kinematic viscosity at 50°C is 119.6mm 2 / s, 88.6mm 2 / s, the API° of hydrogen-donating thermal cracking oil and upgraded oil are 11.3° and 12.5°.
Embodiment 2
[0035] Hydrocarbon feedstock B (a vacuum residue, wherein saturated content 19.89wt%, aromatics 37.58wt%, colloid 29.33wt%, asphaltenes 13.20wt%, Ni+V metal content is 524μg / g, sulfur, Nitrogen contents were 3.26wt%, 0.72wt%, respectively). The addition of hydrogen donor HDB was carried out in a small test in the laboratory. The reaction temperature was 425°C, the reaction was 0.4MPa(G), and the reaction time was 5min. As a result, the spot test grade of the obtained hydrogen-donating thermal cracking oil is grade 2, and the kinematic viscosity at 50°C is 1502.6mm 2 / s, API° is 10.6°, the spot test grade of hydrothermal cracking upgraded oil is grade 1, and the kinematic viscosity at 50°C is 128.3mm 2 / s, API° is 14.7°.
Embodiment 3
[0038]Hydrocarbon feedstock B (a vacuum residue, wherein saturated content 19.89wt%, aromatics 37.58wt%, colloid 29.33wt%, asphaltenes 13.20wt%, Ni+V metal content is 524μg / g, sulfur, Nitrogen contents were 3.26wt%, 0.72wt%, respectively). Add hydrogen donor HDB to carry out continuous device test in the laboratory. The reaction temperature is 423-425°C, the reaction is 0.6MPa(G), and the feed flow rate is 15-18g / min. The properties of the obtained products are shown in Table 3.
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