Inferior diesel oil hydrodesulfurization method
A technology for hydrodesulfurization and low-quality diesel oil, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment. It can solve problems such as poor crude oil quality, reduced processing capacity, and harsh reaction conditions, so as to save investment costs and facilitate transformation. , the effect of high operational flexibility
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Embodiment 1
[0030] In this example, the raw material oil 1 is imported straight-run diesel oil, and its properties are shown in Table 1. Under the process conditions in Table 2, after the raw material oil 1 is mixed with hydrogen, it passes through four reaction zones in sequence, and the reaction effluent enters the separation system after cooling to obtain hydrogen-containing gas and liquid products, and the obtained gas removes H 2 S and NH 3 After recycling, the obtained liquid product enters the fractionation system to obtain refined diesel oil. The catalyst loading volume ratio of the four reaction zones is 2:3:4:1, and the volume ratio of the first type catalyst to the second type catalyst in the second reaction zone is 1:1. In this example, the sulfur content of the diesel product obtained is 32 μg / g, meeting the requirements of the Euro IV standard.
[0031]
Embodiment 2
[0033] In this example, the raw material oil 1 is imported straight-run diesel oil, and its properties are shown in Table 1. Under the process conditions in Table 2, after the raw material oil 1 is mixed with hydrogen, it passes through four reaction zones in sequence, and the reaction effluent enters the separation system after cooling to obtain hydrogen-containing gas and liquid products, and the obtained gas removes H 2 S and NH 3 After recycling, the obtained liquid product enters the fractionation system to obtain refined diesel oil. The catalyst loading volume ratio of the four reaction zones is 2:3:4:1, and the volume ratio of the first type catalyst to the second type catalyst in the second reaction zone is 1:1. In this example, the sulfur content of the diesel product obtained was 9 μg / g, meeting the requirements of the Euro V standard.
[0034]
Embodiment 3
[0036] In this example, the raw material oil 2 is imported straight-run diesel mixed with part of the secondary processing oil, and its properties are shown in Table 1. Under the process conditions in Table 2, after the raw material oil 2 is mixed with hydrogen, it passes through four reaction zones in sequence, and the reaction effluent enters the separation system after cooling to obtain hydrogen-containing gas and liquid products, and the obtained gas removes H 2 S and NH 3 After recycling, the obtained liquid product enters the fractionation system to obtain refined diesel oil. The catalyst loading volume ratio of the four reaction zones is 2:2:5:1, and the volume ratio of the first type catalyst to the second type catalyst in the second reaction zone is 1:1. In this example, the sulfur content of the diesel product obtained is 28 μg / g, meeting the requirements of the Euro IV standard.
[0037]
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