Middle-pressure hydrocracking method for producing aviation kerosene and low-freezing point diesel
A technology for hydrocracking and diesel oil, which is applied in hydrotreating process, petroleum industry, processing hydrocarbon oil, etc., can solve the problem of not being qualified, and achieve the effect of high smoke point, simple process, low equipment investment and operating cost
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Embodiment 1
[0043] At reaction pressure 8.0MPa, refining section reaction temperature 373℃, cracking section reaction temperature 366℃, volumetric space velocity 1.2h -1 / 2.0h -1 , Under the reaction conditions of the hydrogen-to-oil volume ratio of 1200, the hydrorefining catalyst and the hydrocracking catalyst C are used for the reaction, the reaction raw material is raw material A, and the process flow is one pass. The distribution results of the liquid hydrocarbon products obtained by the reaction are shown in Table 2. The properties of jet fuel and diesel oil fractions obtained by cutting liquid hydrocarbon products are listed in Table 3.
Embodiment 2
[0048] At reaction pressure 10.0MPa, refining section reaction temperature 374℃, cracking section reaction temperature 365℃, volumetric space velocity 1.2h -1 / 2.0h -1 , Under the reaction conditions of the hydrogen-to-oil volume ratio of 1200, the hydrorefining catalyst and the hydrocracking catalyst C are used to hydrogenate the raw material B, and the process flow is one pass. The distribution results of liquid hydrocarbon products are shown in Table 4; the liquid hydrocarbon products are cut, and the properties of jet fuel and diesel distillate products are listed in Table 5.
PUM
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