A diesel ultra-deep desulfurization system
A technology for deep desulfurization and diesel oil, which is applied in the treatment of hydrocarbon oil, petroleum industry, organic compound/hydride/coordination complex catalyst, etc., to achieve the effect of improving operation cycle, low hydrogen consumption and high economy
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Embodiment 1
[0048] A high-sulfur straight-run diesel oil distillate from the Middle East is used as the raw material 1, and its properties are shown in Table 1. The raw material oil 1 is mixed with the reactor effluent and hydrogen in the raw material treatment area, and the mixed material is introduced into the first reactor equipped with catalyst D1. In the liquid phase reactor of the first hydrogenation reaction zone, the deep hydrogenation desulfurization reaction is carried out, the reaction conditions are: reaction temperature 360 ℃, raw material oil liquid hourly volume space velocity 2.2h -1 , the reaction system pressure is 8.0MPa.
[0049] The effluent from the first reaction zone enters the high-temperature and high-pressure separation zone and is fed with hydrogen for stripping. The operating conditions are: 320°C, 8.0MPa, hydrogen-to-oil ratio 6.0Nm 3 / m 3 , the liquid phase separated by the high-temperature and high-pressure separator, part of which is recycled back to th...
Embodiment 2
[0059] A mixture of Middle East high-sulfur straight-run diesel fraction and secondary processed FCC diesel fraction is used as feedstock 2, and its properties are shown in Table 1. The reaction system provided by the invention is used for processing. The first hydrogenation reaction zone is equipped with a liquid-phase hydrogenation reactor, filled with hydrogenation refining catalyst D1, and the reaction conditions are: reaction temperature 365 ° C, raw material oil liquid hourly volume space velocity 1.6h -1 , the reaction system pressure is 8.0MPa. Hydrofining catalyst D1 has 3 beds in the reactor, wherein the volume of 1 bed is 15%, the volume of 2 beds is 30%, and the volume of 3 beds is 55%. There is a mixer to mix the reactor flow with hydrogen. The concentration of hydrogen in the reactor stream at the outlet of bed 1 is greater than 5×10 -4 g H 2 / g, there is no need to mix with external hydrogen in the mixer.
[0060] The effluent from the first reactor enters ...
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