Method for producing low-aromatics solvent oil by hydrogenation
A technology of solvent oil and hydrogenation treatment, which is applied in the petroleum industry and the treatment of hydrocarbon oil, etc. It can solve the problems of difficulty in guaranteeing the operation cycle, failure to meet the quality index requirements of high-grade low-aromatic solvent oil, easy poisoning and deactivation, etc.
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Embodiment 1
[0028] The kerosene fraction raw material 1 goes through the heating furnace to reach the required temperature and fully mixes and dissolves the hydrogen in the SH-type static mixer, and then enters the hydrogenation reactor. The reaction conditions are: hydrogen partial pressure 12.8MPa, volume space velocity 0.7h -1 , The reaction temperature is 286° C., and the volume ratio of hydrogen to oil is 150:1. The raw material oil properties and product properties are listed in Table 2.
[0029] It can be seen from Table 2 that the sulfur and nitrogen content of the solvent oil product can be reduced to below 1 μg / g, and the aromatic hydrocarbon content is less than 0.05%.
Embodiment 2
[0031] The kerosene fraction raw material 2 is fully mixed with hydrogen and enters the hydrogenation reactor after passing through the heating furnace. The gas-liquid mixer adopts SK type static mixer. The reaction conditions are: hydrogen partition pressure 12.5MPa, volume space velocity 0.6h -1 , The reaction temperature is 281° C., and the volume ratio of hydrogen to oil is 140:1. The raw material oil properties and product properties are listed in Table 3.
[0032] It can be seen from Table 3 that the sulfur and nitrogen content of the solvent oil product can be reduced to less than 1 μg / g, and the aromatic hydrocarbon content is less than 0.05% by using this process technology.
Embodiment 3
[0034] The kerosene fraction raw material 3 is fully mixed with hydrogen and enters the hydrogenation reactor after passing through the heating furnace. The reaction conditions are: hydrogen partial pressure 13.6MPa, volume space velocity 0.8h -1 , The reaction temperature is 304°C, and the volume ratio of hydrogen to oil is 170:1. Half of the hydrogen is mixed with the raw materials through the SL gas-liquid mixer, and the other half is directly fed into the reactor through the pipeline. The raw material oil properties and product properties are listed in Table 4.
[0035] It can be seen from Table 4 that the sulfur and nitrogen content of the solvent oil product can be reduced to less than 1 μg / g, and the aromatic hydrocarbon content is less than 0.05%.
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