Method of preparing needle coke raw oil from oil slurry
A technology for needle coke and raw oil, applied in the petrochemical field, can solve the problems of high asphaltene content, low economic value, waste of resources, etc., and achieve the effects of high asphaltene content, low aromatic content and cost reduction.
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Embodiment 1
[0027] A method for preparing needle coke raw material oil from oil slurry, the preparation steps are as follows:
[0028] In the first step, the oil slurry is deasphaltenized, the volume ratio of n-hexane and oil slurry is 3:1, stirred at 20°C for 50 minutes, and the upper layer is taken after standing still; in the second step, solvent extraction is carried out, and the furfural and oil slurry The ratio is 2:1, stirred at 20°C for 20 minutes, and the lower layer is taken after standing still; the third step is to desolidify, and use a disc centrifuge with a separation factor of 6000 to perform centrifugal desolidification at 40°C, and the fourth step is to desolidify The desolidified oil slurry is subjected to solvent removal treatment, and different side lines are set up to collect n-hexane, light components in the oil slurry, and furfural; the fifth step is to carry out hydrogenation treatment on the oil slurry to remove sulfur and nitrogen, and the reaction temperature is ...
Embodiment 2
[0030] A method for preparing needle coke raw material oil from oil slurry, the preparation steps are as follows:
[0031] In the first step, the oil slurry is deasphaltenized, the volume ratio of n-pentane to oil slurry is 7:1, stirred at 40°C for 30 minutes, and the upper layer is taken after standing; the second step is solvent extraction, N-methyl The ratio of pyrrolidone to oil slurry is 6:1, stir at 35°C for 20 minutes, and take the lower layer after standing; the third step is to desolidify, and use a disc centrifuge with a separation factor of 8000 to perform centrifugal desolidification at 20°C In the fourth step, the oil slurry after desolidification is desolvated, and different side lines are set to collect n-pentane, light components in the oil slurry, and N-methylpyrrolidone; the fifth step is to carry out hydrogenation treatment to the oil slurry, To remove sulfur and nitrogen, the reaction temperature is 440°C, the reaction pressure is 10MPa, and the space veloc...
Embodiment 3
[0033] A method for preparing needle coke raw material oil from oil slurry, the preparation steps are as follows:
[0034] In the first step, the oil slurry is deasphaltenized, the volume ratio of n-heptane and oil slurry is 5:1, stirred at 30°C for 40 minutes, and the upper layer is taken after standing; the second step is solvent extraction, sulfolane and oil slurry The ratio is 4:1, stirred at 40°C for 40min, and the lower layer was taken after standing; the third step is desolidification, using a disc centrifuge with a separation factor of 7000 to carry out centrifugal desolidification at 30°C, the fourth step The desolidified oil slurry is subjected to solvent removal treatment, and different side lines are set to collect n-heptane, light components in the oil slurry, and sulfolane; the fifth step is to carry out hydrogenation treatment on the oil slurry to remove sulfur and nitrogen, and the reaction temperature is 400°C, reaction pressure 12MPa, space velocity 2h -1 , ...
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