A method for producing clean diesel
A diesel and clean technology, which is applied in the treatment of hydrocarbon oil, petroleum industry, hydrocarbon oil treatment products, etc., can solve the problems of the difficulty of the ultra-deep hydrodesulfurization method of secondary processing diesel oil, and achieves the promotion of the hydrotreating of residual oil to remove impurities. The effect of reaction, reducing coking, and prolonging the operation period
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Embodiment 1
[0036] Straight-run diesel oil A, light secondary processed diesel fraction B1, and diesel fraction I produced by the residual oil hydrogenation unit are mixed with hydrogen and enter the diesel hydrogenation unit together, and undergo deep hydrodesulfurization under the action of a hydrofining catalyst. The conditions are: the reaction temperature is 345°C, the volumetric space velocity of the raw material oil is 1.5h -1 , the hydrogen partial pressure is 6.4MPa, and the hydrogen-to-oil ratio is 500. The reactor effluent was separated to obtain diesel fraction II, and its product properties are shown in Table 2.
[0037] Residual oil raw material D, heavy secondary processed diesel fraction B2 are mixed with hydrogen and enter the residual oil hydrogenation reactor together, and react under the action of residual oil hydrogenation catalyst. The reaction conditions are reaction temperature 395°C, volume of raw oil Airspeed 0.237h -1 , the hydrogen partial pressure is 17.0MPa...
Embodiment 2
[0053] Straight-run diesel oil A, light secondary processed diesel fraction C1, and diesel fraction I produced by the residual oil hydrogenation unit are mixed with hydrogen and then enter the diesel hydrogenation unit together, and undergo deep hydrodesulfurization under the action of a hydrofining catalyst. The conditions are: the reaction temperature is 353°C, the volumetric space velocity of the raw material oil is 1.5h -1 , the hydrogen partial pressure is 6.4MPa, and the hydrogen-to-oil ratio is 500. The reactor effluent was separated to obtain diesel fraction II, and its product properties are shown in Table 2.
[0054] Residual oil D and heavy secondary processed diesel fraction C2 are mixed with hydrogen and enter the residual oil hydrogenation reactor together, and react under the action of residual oil hydrogenation catalyst. 0.23h -1 , the hydrogen partial pressure is 17.0MPa, and the hydrogen-to-oil ratio is 600. The reactor effluent was separated to obtain gas...
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