Method of preparing mesophase pitch by means of naphthene-based vacuum gas oil co-carbonization
A technology of mesophase pitch and co-carbonization, which is applied in the processing of tar pitch/petroleum pitch/natural pitch, chemically processing tar pitch/petroleum pitch/natural pitch, petroleum industry, etc., can solve the problem of light components hindering mesophase Due to the large amount of asphalt and hydrogen-supplying solvent added, and the high cost of cross-linking agent, it can achieve the effect of improving the effect, ensuring the yield and anti-oxidation performance, and improving the softening point.
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Embodiment 1
[0033] The furfural extracted oil of the vacuum distillate oil of Huanxiling crude oil in Liaohe Oilfield (the kinematic viscosity is 200.6mm at 40°C) 2 / s, aromatics content 65.7wt%, cycloalkane content 31.5wt%, paraffin content 2.8wt%) 300g add volume and be in the stainless steel autoclave of 500ml. When the temperature in the reaction kettle rose to 130°C, air was blown into the raw material, the flow rate was 100mL / (h g), the reaction temperature was 250°C, and the temperature was kept constant for 5 hours. At this time, the softening point of the raw material after crosslinking was 141°C. During the reaction, keep the reaction system at normal pressure (1 atmospheric pressure); then stop venting the air, add 30g (10wt% of raw material addition) of 1,2,3,4-tetrahydroquinoline in the reactor, then use hydrogen Replace the air in the reactor, and then fill it with hydrogen, so that the pressure inside the reactor is 3MPa, seal the reactor; start stirring, the rotation speed ...
Embodiment 2
[0035] Extract the furfural oil of Huanxiling crude oil decompression distillate from Liaohe Oilfield (kinematic viscosity 136.9mm at 40°C) 2 / s, aromatics content 58.3wt%, cycloalkane content 38.5wt%, paraffin content 2.6wt%) 300g add volume and be in the stainless steel autoclave of 500ml. When the temperature in the reaction kettle rose to 130°C, air with a flow rate of 170mL / (h g) was blown into the raw material under normal pressure. After 6 hours of reaction at 280°C, the softening point of the raw material rose to 158°C; Then stop venting air, add 60g (20wt% of raw material addition) 1,2,3,4-tetrahydroquinoline in reactor, after replacing the air in reactor with hydrogen, charge into hydrogen again, make The pressure in the reactor is 5MPa, and the reactor is closed; start stirring, the speed is 800r / min, and the temperature is raised to 400°C for 8 hours. Introduce hydrogen, and stabilize the pressure of the system at 4.5 MPa through the back pressure valve. After con...
Embodiment 3
[0037] Extract the furfural oil (kinematic viscosity 287.2mm 2 / s, aromatics content 72.1wt%, cycloalkane content 25.4wt%, paraffin content 2.5wt%) 300g add volume and be in the stainless steel autoclave of 500ml. When the temperature in the reaction kettle rose to 150°C, air with a flow rate of 80mL / (h g) was blown into the raw material under normal pressure. After 6 hours of reaction at 250°C, the softening point of the raw material rose to 146°C; Then stop venting air, add 60g (20wt% of raw material addition) 1,2,3,4-tetrahydroquinoline in reactor, after replacing the air in reactor with hydrogen, charge into hydrogen again, make The pressure in the reactor is 5MPa, and the reactor is closed; start stirring, the speed is 1000r / min, the temperature is raised to 450°C, and the reaction is carried out for 5 hours. Pass hydrogen into the middle, and stabilize the pressure of the system at 5 MPa through the back pressure valve, continue the reaction for 5 hours, stop the hydrog...
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