Hydrocracking method of low-energy-consumption, productive and high-quality jet fuel
A technology for hydrocracking and jet fuel, which is applied in the field of hydrocracking, can solve the problems of large circulation of kerosene fractions, increased investment in equipment, complicated operation, etc. The effect of transforming power
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Embodiment 1-3
[0041] Embodiment 1-3 adopts figure 1 In the schematic process shown, all the tail oil is recycled to the second hydrocracking reaction zone. The properties of the raw oil used are shown in Table 1. FF-46 hydrogenation pretreatment catalyst and different volume ratios of hydrocracking catalyst I / hydrogenation The cracking catalyst II catalyst system, the composition and properties of the catalyst are shown in Table 2. The process conditions and product properties of Examples 1 to 3 are listed in Tables 3 and 4. The distillation ranges of each fraction in the examples are: heavy naphtha 65-160°C, middle distillates 160-300°C, tail oil>300°C ℃.
[0042] The first stage mentioned in the embodiment refers to the single-stage series reaction zone formed by the hydroprocessing reaction zone and the first hydrocracking reaction zone; the second stage refers to the second hydrocracking reaction zone.
[0043] The results of Examples 1-3 show that, by adopting the hydrocracking metho...
Embodiment 4-5
[0058] Embodiment 4-5 adopts figure 1 In the schematic process shown, the tail oil is partially recycled, and the circulation amount is 50% of the generated tail oil. The feedstock oil and catalyst system are the same as those in Examples 1-3. The process conditions and product properties are listed in Table 6. The distillation ranges of each fraction in the examples are: heavy naphtha 65-160°C, middle distillate 160-330°C, and tail oil >330°C.
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