Method for producing high-octane number gasoline by poor-quality diesel oil
A technology for high-octane gasoline and low-quality diesel, which is applied in the petroleum industry, hydrocarbon oil treatment, hydrotreating process, etc., and can solve the problem of low octane number and liquid yield of gasoline, poor extraction effect, low octane number, etc. problems, to achieve the effects of high aromatics selectivity, full conversion, and improved utilization.
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Embodiment 1
[0032] Adopt the method provided by the present invention to process straight-run diesel oil, first carry out hydrofinishing, the process condition of hydrofinishing is temperature 360 ℃, pressure 6.0MPa, volumetric space velocity 1.0h -1 , hydrogen-to-oil ratio 600; hydrofined products are collected for dehydrogenation reaction, the reaction process conditions are temperature 420°C, pressure 3.0MPa, volume space velocity 1.0h -1 , hydrogen-to-oil ratio 400; dehydrogenation product oil enters heavy aromatics lightening reaction section for selective hydrocracking reaction, the reaction process conditions are temperature 420°C, pressure 3.0MPa, volume space velocity 1.0h -1, the hydrogen-to-oil ratio is 600, and the light products of heavy aromatics are cut and fractionated, and the fraction below 205°C is recovered as the product; the fraction above 205°C is mixed into the dehydrogenation product oil according to the conversion ratio for cyclic reaction, and the material is c...
Embodiment 2
[0034] The same as in Example 1, except that the hydrofined product is not dehydrogenated and directly enters the heavy aromatics lightening reaction section for reaction. The reaction process conditions and product distribution are shown in Table 2.
Embodiment 3
[0036] Same as Example 1, except that the processed raw material is changed to FCC diesel oil, and the reaction process conditions and product distribution are shown in Table 2.
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