Low energy consumption hydrocracking method for producing high-quality jet fuel
A technology of hydrocracking and jet fuel, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment, etc. It can solve the problems of unreasonable use of hydrocracking reaction heat, large circulation of kerosene fraction, and decrease of API degree, etc. Achieve the effects of small footprint, reduced engineering investment, and fewer units used
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Embodiment 1~3
[0031] Using Iranian VGO as feedstock oil, the catalyst system of sulfurized FF-46 hydrocracking pretreatment catalyst and sulfurized hydrocracking catalyst I / sulfurized hydrocracking catalyst II in different volume ratios was selected. Catalyst Ⅰ and catalyst Ⅱ are both supported by amorphous silica-alumina and modified Y molecular sieve. The volume ratios of hydrocracking catalyst I / hydrocracking catalyst II in Examples 1-3 are 2:1, 1:1 and 1:2, respectively.
[0032] At a total reaction pressure of 15.7MPa, the volume ratio of hydrogen to oil in the refining section and the cracking section is 900:1 and 1200:1 respectively, and the volume space velocity of the refining section and the cracking section are 1.0h -1 and 1.5h -1 , control the nitrogen content of refined oil to 5-8 μg×g -1 , a process test with a conversion rate of about 80wt% at >350°C was carried out, and the product quality of each fraction was investigated.
Embodiment 4
[0046] According to the complete set of hydrogenation technology of the present invention, newly build a set of 2 million tons / year hydrocracking unit, carry out economic calculation and can obtain following conclusion:
[0047] (1) Specific comparison results with conventional hydrocracking unit project investment:
[0048] 1. The investment of high-pressure heat exchanger was reduced by 4.9 million yuan;
[0049] 2. The investment in reaction feed heating furnace was reduced by 9.24 million yuan;
[0050] 3. The investment of thermal high-separation air-air cooler was reduced by 8.2 million yuan;
[0051] 4. The investment in circulating hydrogen compressor is reduced by 500,000 yuan;
[0052] The total investment in installation projects decreased by 22.84 million yuan, a decrease of 4.56%.
[0053] (2) Compared with the fuel consumption of conventional hydrocracking units, the results are as follows:
[0054] 1. The fuel consumption of the reaction feed heating furnace...
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