Diesel oil deep hydrodesulfurization method
A deep hydrogenation and diesel oil technology, which is applied in the fields of hydrogenation treatment process, petroleum industry, and hydrocarbon oil treatment, can solve the problems of not being able to meet the product chromaticity index at the same time, so as to save investment and operating costs, reduce usage, improve The effect of product color
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Embodiment 1
[0038] The raw material oil A and hydrogen enter into the reactor equipped with hydrogenation catalyst C together, and the volume ratio of hydrogen to oil is 300Nm 3 / m 3 , under the action of hydrogenation catalyst C, a deep hydrodesulfurization reaction is carried out. The reaction conditions are: the reaction temperature is 380 °C, and the volumetric space velocity of the raw oil is 3.0h. -1 , the pressure of the reaction system is 6.0 MPa, and the sulfur content of the liquid-phase stream in the obtained reactor effluent is less than 10 μg / g.
[0039] The middle part of the hot high pressure separator is filled with hydrogenation catalyst D, and the effluent from the reactor enters the hot high pressure separator from the upper part of the hot high pressure separator through heat exchange, and passes through the catalyst bed packed in the hot high pressure separator from top to bottom. The temperature of the separator is 300℃, the pressure is 6.0MPa, and the liquid hourly...
Embodiment 2
[0041] The raw material oil B and hydrogen enter into the reactor equipped with hydrogenation catalyst C together, and the volume ratio of hydrogen to oil is 500Nm 3 / m 3 , under the action of hydrogenation catalyst C, the deep hydrodesulfurization reaction is carried out. -1 , the reaction system pressure is 8.0MPa.
[0042] The middle of the hot high pressure separator is filled with hydrogenation catalyst C, and the effluent from the reactor enters the hot high pressure separator from the bottom of the hot high pressure separator through heat exchange, and passes through the catalyst bed packed in the hot high pressure separator from bottom to top. The temperature of the separator is 270℃, the pressure is 8.0MPa, and the liquid hourly volume space velocity is 18.0h -1 . The liquid phase stream separated by the hot high pressure separator is cooled and separated to obtain hydrogenated gasoline and hydrogenated diesel oil. The reaction conditions and hydrogenated diesel p...
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